WO2012088650A1 - Regenerative absorbing/generating system and regenerative third-type absorption heat pump - Google Patents

Abstract

Disclosed are a regenerative absorbing/generating system and a regenerative third-type absorption heat pump. The main components of the regenerative absorbing-generating system include an absorption-evaporator (1), an absorber (2), a first absorption-generator (3), a second absorption-generator (4), a generator (5), a number of solution pumps, a number of solution heat exchangers, a first vapor separating chamber (11), and a second vapor separating chamber (12), or further include a solution throttle valve (14), and constitute a solution circulation of single way or of double ways. The absorption-evaporator (1), the first absorption-generator (3) and the second vapor separating chamber (12) constitute a regenerative fluid path, and the second absorption-generator (4) and the first vapor separating chamber (11) constitute a solution generating fluid path depending on a second-type driving power, and the generator (5) constitutes a solution generating fluid path depending on a first-type driving power, thereby a regenerative absorbing/generating system is formed. The regenerative absorption heat pump is formed by adding a first condenser (16), a second condenser (17), a first evaporator (18), throttle valves and coolant pumps, or further adding a second evaporator (19) to the regenerative absorbing/generating system.

Description

 The invention relates to a regenerative absorption-generation system and a regenerative third-type absorption heat pump. Technical Field - The invention belongs to the technical field of low-temperature waste heat utilization heat pump.

Background technique:

 For the third type of absorption heat pumps with different efficacies or different series, their working parameter intervals are not connected, and there is a big difference in the performance index.

 From the perspective of the workflow, in order to improve the maximum heating temperature of the third type of absorption heat pump, the key is to reduce the concentration of the solution entering the generator; in order to utilize the lower temperature waste heat resource, the key is to increase the concentration of the dilute solution at the outlet of the absorber. . It is very important to take reasonable technical measures to increase the concentration of the dilute solution at the outlet of the absorber and to reduce the concentration of the solution entering the generator, and to select the solution concentration and the extent of the solution according to the demand within a certain range. .

 In order to improve the heating temperature of the third type of absorption heat pump, to have a higher performance index and to achieve an uninterrupted connection between the operating parameters and the performance index, the present invention employs a clever process to apply the regenerative principle. The absorption-accumulation process of the solution, the absorption-evaporator and the first absorption-generator constitute a regenerative process, and a regenerative absorption-generation system is established; and based on the regenerative absorption-generation system, the increase includes the first a condenser, a second condenser, a first evaporator or a related component including a second evaporator, a throttle valve and a refrigerant liquid pump, and a regenerative third type with different effectiveness and different stages Absorption heat pump, so that each working parameter interval has a corresponding third type of absorption heat pump, to realize the continuity of the third type of absorption heat pump in the working parameter interval, and realize the performance index of the third type of absorption heat pump. Continuous.

Summary of the invention:

 The main object of the present invention is to provide a regenerative absorption-generation system and a regenerative third-type absorption heat pump, including four regenerative absorption-generation systems and a series of regenerative types based on a regenerative absorption-generation system. The third type of absorption heat pump. The specific content of the invention is described as follows:

 1. A regenerative absorption-generation system, which is mainly composed of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, and a third a solution pump, a first solution heat exchanger, a second solution heat exchanger, a first steam dividing chamber and a second steam dividing chamber, the absorption-evaporator having a dilute solution pipeline passing through the third solution pump and the first absorption-occurring The first absorption-generator and the dilute solution pipeline are connected to the first steam separation chamber via the second solution heat exchanger and the second absorption-generator, and the first steam distribution chamber has a concentrated solution pipeline The second solution pump, the second solution heat exchanger and the first absorption-generator are in communication with the second steam separation chamber, and the second steam separation chamber has a concentrated solution line connected to the absorber, and the absorber has a dilute solution line and The absorption-evaporator is connected, the second absorption-generator has a dilute solution line connected to the generator via the first solution pump and the first solution heat exchanger, and the generator has a concentrated solution line through the first solution heat exchanger and Second absorption-generator connection, absorption-evaporator and coolant The steam passage communicates with the outside or there is a refrigerant vapor passage to communicate with the outside and a heated medium conduit to communicate with the outside, and the external refrigerant liquid pipeline communicates with the absorption-evaporator to absorb the vaporizer and then the refrigerant vapor. The passage is connected to the first absorption-generator, and the absorber further has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, and the second steam distribution chamber also has a refrigerant vapor passage connected to the absorption-evaporator. The first steam dividing chamber also has a refrigerant vapor passage communicating with the outside or respectively having a refrigerant vapor passage communicating with the outside and a cooling medium conduit communicating with the outside, and the second absorption-generator also has a refrigerant vapor passage and an external portion. Connected or also have a refrigerant vapor passage to communicate with the outside and a heated medium conduit to communicate with the outside, and the generator also has a refrigerant vapor passage to communicate with the outside and a drive heat medium conduit to communicate with the outside to form a two-way circulation. Regenerative absorption-generation system; wherein, the solution throttle valve can be used instead of the second solution heat exchanger, and the first absorption-generator has a dilute solution pipeline through the second The solution heat exchanger and the second absorption-generator are connected to the first distribution chamber to be changed to a first absorption-generator having a dilute solution line connected to the first distribution chamber via the solution throttle valve and the second absorption-generator , the first solution compartment has a concentrated solution pipeline through the second solution pump, the second solution heat exchanger and the first absorption-generator and the second separation chamber are changed to the first distribution chamber and the concentrated solution pipeline The second solution pump and the first absorption-generator are in communication with the second distribution chamber.

2. Regenerative absorption-generation system, which is mainly composed of absorption-evaporator, absorber, first absorption-generator, second suction The specification includes a generator, a generator, a first solution pump, a second solution pump, a third solution pump, a first solution heat exchanger, a second solution heat exchanger, a first distribution chamber, a second distribution chamber, The fourth solution pump and the solution throttle valve are composed, the absorption-evaporator has a dilute solution pipeline connected to the first absorption-generator via the third solution pump, and the first absorption-generator and the dilute solution pipeline pass the second solution The heat exchanger and the second absorption-generator are in communication with the first steam dividing chamber, and the first steam dividing chamber further has a concentrated solution line passing through the second solution pump, the second solution heat exchanger and the first absorption-generator and the first The second steam chamber is connected, the second steam chamber and the concentrated solution pipeline are connected to the absorber through the fourth solution pump, and the absorber and the dilute solution pipeline are connected to the absorption-evaporator through the solution throttle, the second absorption - the generator has a dilute solution line connected to the generator via the first solution pump and the first solution heat exchanger, and the generator and the concentrated solution line are connected to the second absorption-generator via the first solution heat exchanger, absorbing - the evaporator also has a refrigerant vapor channel connected to the outside and has The heating medium pipeline communicates with the outside, and the external refrigerant liquid pipeline communicates with the absorption-evaporator, and the absorption-vaporizer and the refrigerant vapor passage communicate with the first absorption-generator, and the absorber also has a refrigerant vapor passage. Communicating with the outside and having a heated medium line communicating with the outside, the second steam dividing chamber also has a refrigerant vapor passage communicating with the absorption-evaporator, and the first steam dividing chamber and the refrigerant vapor passage are connected to the outside or respectively The refrigerant vapor passage communicates with the outside and has a cooling medium conduit communicating with the outside, and the second absorption-generator and the refrigerant vapor passage are connected to the outside or respectively have a refrigerant vapor passage communicating with the outside and the heated medium conduit Connected to the outside, the generator also has a refrigerant vapor passage to communicate with the outside and a drive heat medium conduit to communicate with the outside to form a two-way circulation regenerative absorption-generation system: wherein the second solution throttle valve can be selected Substituting the second solution heat exchanger, changing the first absorption-generator dilute solution line to the first absorption chamber via the second solution heat exchanger and the second absorption-generator to the first separation chamber - the generator has a dilute solution line connected to the first steam dividing chamber via the second solution throttle valve and the second absorption-generator, and the first steam dividing chamber has a concentrated solution line through the second solution pump, the second solution The heat exchanger and the first absorption-generator are connected to the second distribution chamber to be changed to the first distribution chamber. The concentrated solution line is connected to the second distribution chamber via the second solution pump and the first absorption-generator.

 3. A regenerative absorption-generation system, which is mainly composed of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, and a third a solution pump, a first solution heat exchanger, a second solution heat exchanger, a first steam dividing chamber and a second steam dividing chamber, the absorption-evaporator having a dilute solution pipeline passing through the third solution pump and the first absorption-occurring Connected, the first absorption-generator and the dilute solution line are connected to the second absorption-generator via the second solution heat exchanger, and the second absorption-generator and the dilute solution line are passed through the first solution pump and a solution heat exchanger is connected to the generator, and the generator and the concentrated solution pipeline are connected to the first steam separation chamber via the first solution heat exchanger and the second absorption generator, and the first steam distribution chamber has a concentrated solution tube The second solution pump, the second solution heat exchanger and the first absorption-generator are in communication with the second steam separation chamber, and the second steam distribution chamber has a concentrated solution line connected to the absorber, and the absorber has a dilute solution. The pipeline is connected to the absorption-evaporator, and the absorption-evaporator is also cooled by steam. The steam passage communicates with the outside or there is a refrigerant vapor passage to communicate with the outside and a heated medium conduit to communicate with the outside, and the external refrigerant liquid pipeline communicates with the absorption-evaporator to absorb the vaporizer and then the refrigerant vapor. The passage is connected to the first absorption-generator, and the absorber further has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, and the second steam distribution chamber also has a refrigerant vapor passage connected to the absorption-evaporator. The first steam dividing chamber also has a refrigerant vapor passage communicating with the outside, and the second absorption-generator and the refrigerant vapor passage are connected to the outside or have a refrigerant vapor passage respectively communicating with the outside and having a heated medium conduit and Externally connected, the generator also has a refrigerant vapor passage to communicate with the outside and a drive heat medium pipeline to communicate with the outside to form a single loop regenerative absorption-generation system; wherein, the solution throttle valve can be used instead of the second a solution heat exchanger, wherein the first absorption-generator has a dilute solution line connected to the second absorption-generator through the second solution heat exchanger to be changed to the first absorption-generator The liquid pipeline is connected to the second absorption-generator via the solution throttle valve, and the first steam distribution chamber has a concentrated solution pipeline through the second solution pump, the second solution heat exchanger, and the first absorption-generator and the second The steam separation chamber is changed to be the first steam distribution chamber. The concentrated solution pipeline is connected to the second steam distribution chamber via the second solution pump and the first absorption generator.

4. A regenerative absorption-generation system, which is mainly composed of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, and a third a solution pump, a first solution heat exchanger, a second solution heat exchanger, a first steam dividing chamber, a second steam dividing chamber, a fourth solution pump and a solution throttle valve, and the absorption-evaporator has a dilute solution line The third solution pump is in communication with the first absorption-generator, the first absorption-generator and the dilute solution line are in communication with the second absorption-generator via the second solution heat exchanger, and the second absorption-generator is also sparse The solution line passes through the first solution pump and the first solution The heat exchanger is connected to the generator, and the generator and the concentrated solution pipeline are connected to the first steam separation chamber via the first solution heat exchanger and the second absorption generator, and the first steam distribution chamber has a concentrated solution pipeline The second solution pump, the second solution heat exchanger and the first absorption-generator are in communication with the second steam separation chamber, and the second distribution chamber and the concentrated solution line are connected to the absorber via the fourth solution pump, and the absorber is further The dilute solution pipeline is connected to the absorption-evaporator through the solution throttle valve, and the absorption-evaporator also has a refrigerant vapor passage to communicate with the outside and a heated medium conduit to communicate with the outside, and the external refrigerant liquid pipeline and After the absorption-evaporator is connected, the absorption-evaporator has a refrigerant vapor passage communicating with the first absorption-generator, and the absorber further has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, second The steam dividing chamber also has a refrigerant vapor passage communicating with the absorption-evaporator, the first steam dividing chamber and the refrigerant vapor passage communicating with the outside, and the second absorption-generator and the refrigerant vapor passage communicating with the outside or respectively Coolant vapor channel is connected to the outside The heated medium pipeline is connected to the outside, and the generator also has a refrigerant vapor passage to communicate with the outside and a driving heat medium pipeline to communicate with the outside to form a single loop regenerative absorption-generation system; The second solution throttle valve replaces the second solution heat exchanger, and the first absorption-generator has a dilute solution line connected to the second absorption-generator through the second solution heat exchanger to be changed to the first absorption-generator The dilute solution line is connected to the second absorption-generator via the second solution throttle valve, and the first distribution chamber has a concentrated solution line through the second solution pump, the second solution heat exchanger and the first absorption-generator The communication with the second steam distribution chamber is changed to the first steam distribution chamber, and the concentrated solution pipeline is connected to the second steam separation chamber via the second solution pump and the first absorption generator.

 5. A regenerative third type absorption heat pump, wherein in the recuperative absorption-generation system according to item 1, the first condenser, the second condenser, the first evaporator, the second evaporator, The throttle valve, the first refrigerant liquid pump and the second refrigerant liquid pump connect the generator refrigerant vapor passage to the outside to determine that the generator has a refrigerant vapor passage communicating with the first condenser, and the first condenser further The refrigerant liquid pipeline is connected to the second evaporator through the throttle valve, and the second absorption-generator has a refrigerant vapor passage communicating with the outside to determine that the second evaporator has a refrigerant vapor passage and a second absorption-generator Connected, the first steam dividing chamber has a refrigerant vapor passage communicating with the outside to determine that the first steam dividing chamber has a refrigerant vapor passage communicating with the second condenser, and the second condenser has a refrigerant liquid pipeline passing through the first cold The agent liquid pump is in communication with the first evaporator, and the absorption-vaporizer has a refrigerant vapor passage communicating with the outside to determine that the first evaporator has a refrigerant vapor passage communicating with the absorption-evaporator, and the absorber has a refrigerant vapor passage and External connection is determined as the first evaporator has a refrigerant vapor The passage is connected to the absorber, and the external refrigerant liquid line is connected to the absorption-evaporator, and the absorption-evaporator and the refrigerant vapor passage are connected to the first absorption-generator to be determined as the first evaporator or the second condenser. The refrigerant liquid pipeline is connected to the absorption-evaporator through the second refrigerant liquid pump, and the absorption-evaporator and the refrigerant vapor channel are connected to the first absorption-generator, and the first condenser has a heated medium pipeline. The second condenser and the cooling medium pipeline are connected to the outside, and the first evaporator and the second evaporator respectively have a residual heat medium pipeline communicating with the outside to form a single-stage single-effect regenerative third-class absorption. Heat pump; wherein, when there is no second evaporator, the first condenser has a refrigerant liquid pipeline connected to the second evaporator through the throttle valve to be changed into a first condenser, a refrigerant liquid pipeline, a throttle valve and a An evaporator is connected, and the first evaporator increases the refrigerant vapor passage to communicate with the second absorption-generator.

6. A regenerative third type absorption heat pump, wherein in the regenerative absorption-generation system according to item 2, the first condenser, the second condenser, the first evaporator, the second evaporator, a third evaporator, a first throttle, a second throttle, a first refrigerant liquid pump and a second refrigerant liquid pump, and the generator has a refrigerant vapor passage connected to the outside to determine that the generator has refrigerant vapor The passage is in communication with the first condenser, the first condenser and the refrigerant liquid pipeline are connected to the second evaporator via the first throttle valve, and the second absorption-generator has a refrigerant vapor passage communicating with the outside to determine The second evaporator has a refrigerant vapor passage communicating with the second absorption-generator, and the first steam distribution chamber has a refrigerant vapor passage communicating with the outside to determine that the first steam distribution chamber has a refrigerant vapor passage communicating with the second condenser. The second condenser further has a refrigerant liquid pipeline connected to the first evaporator via the first refrigerant liquid pump, and the first evaporator and the refrigerant liquid pipeline are connected to the third evaporator via the second throttle valve, The absorption-evaporator has a refrigerant vapor passage connected to the outside to determine that the third evaporator has a refrigerant The steam passage is in communication with the absorption-evaporator, and the refrigerant vapor passage of the absorber is communicated with the outside to determine that the first evaporator has a refrigerant vapor passage communicating with the absorber, and the external refrigerant liquid conduit is connected to the absorption-evaporator. The post-absorption-evaporator and then the refrigerant vapor channel are connected to the first absorption-generator to determine that the third evaporator or the first evaporator has a refrigerant liquid line that is connected to the absorption-evaporator via the second coolant pump. The absorption-evaporator further has a refrigerant vapor passage communicating with the first absorption-generator, the first condenser and the heated medium conduit communicating with the outside, and the second condenser having a cooling medium conduit and Externally connected, the first evaporator, the second evaporator and the third evaporator respectively have a residual heat medium pipeline communicating with the outside to form a single-stage single-effect regenerative third-type absorption heat pump; wherein, there is no second evaporator When the first condenser has a refrigerant liquid pipeline connected to the second evaporator through the first throttle valve to be changed into a first condenser, the refrigerant liquid pipeline is connected to the first evaporator through the first throttle, and the first An evaporator increases the refrigerant vapor passage in communication with the second absorption-generator.

 7. The regenerative third type absorption heat pump is a regenerative absorption-generation system in which the second absorption-generator has a medium to be heated and communicated with the outside, and the first condenser is added. a second condenser, a first evaporator, a second evaporator, a first refrigerant liquid pump, a second refrigerant liquid pump or a third throttle valve, a first throttle valve and a second throttle valve, which will occur The refrigerant vapor passage is connected to the outside to determine that the generator has a refrigerant vapor passage communicating with the first condenser, and the first condenser and the refrigerant liquid pipeline are connected to the first evaporator via the first throttle valve, The first steam dividing chamber has a refrigerant vapor passage communicating with the outside to determine that the first steam dividing chamber has a refrigerant vapor passage communicating with the second condenser, and the second condenser has a refrigerant liquid pipeline passing through the first refrigerant liquid pump. Communicating with the first evaporator or the second evaporator, the first evaporator and the refrigerant liquid pipeline are connected to the second evaporator via the second section, and the second absorption-generator has a refrigerant vapor passage and the outside The connection is determined to be that the second evaporator has a refrigerant vapor passage communicating with the second absorption-generator, The absorption-evaporator has a refrigerant vapor passage communicating with the outside to determine that the first evaporator has a refrigerant vapor passage communicating with the absorption-evaporator, and the absorber has a refrigerant vapor passage communicating with the outside to determine that the first evaporator is cold. The vapor channel of the agent is in communication with the absorber, and the external refrigerant liquid line is connected to the absorption-evaporator, and the absorption-evaporator and the refrigerant vapor channel are connected with the first absorption-generator to determine that the first evaporator has a refrigerant. The liquid pipeline is connected to the absorption-evaporator through the second refrigerant liquid pump, and then the absorption-vaporizer and the refrigerant vapor passage are connected to the first absorption-generator, or it is determined that the first condenser has a refrigerant liquid pipeline. The third throttle valve is connected to the absorption-evaporator, and the absorption-evaporator is further connected to the first absorption-generator via a refrigerant vapor passage, and the first condenser and the heated medium conduit are connected to the outside, the second condenser The cooling medium pipeline is connected to the outside, and the first evaporator and the second evaporator respectively have a residual heat medium pipeline communicating with the outside to form a single-stage single-effect regenerative third-type absorption heat pump; wherein: 1 Two evaporator The second condenser has a refrigerant liquid pipeline connected to the first evaporator or the second evaporator via the first refrigerant liquid pump to determine that the second condenser has a refrigerant liquid pipeline through the first refrigerant liquid pump and the first An evaporator is connected to cancel the refrigerant liquid line of the first evaporator connected to the second evaporator via the second throttle valve, and the first evaporator increases the refrigerant vapor channel to communicate with the second absorption-generator; The first condenser has a refrigerant liquid pipeline connected to the first evaporator through the first section to be adjusted to be the first condenser, and the refrigerant liquid pipeline is connected to the second evaporator through the first throttle valve, and The first evaporator has a refrigerant liquid pipeline connected to the second evaporator via the second throttle valve to be adjusted to be a second evaporator. The refrigerant liquid pipeline is connected to the first evaporator via the second throttle valve.

8. The regenerative third type absorption heat pump is a regenerative absorption-generation system in which the second absorption-generator is connected to the outside without the heated medium line, and the first condenser is added. a second condenser, a first evaporator, a second evaporator, a first refrigerant liquid pump, a first throttle, a second refrigerant pump or a second throttle valve, and the generator has a refrigerant vapor passage The communication with the outside is determined to be that the generator has a refrigerant vapor passage communicating with the first condenser, and the first condenser and the refrigerant liquid pipeline are connected to the first evaporator via the first throttle valve, and the first steam compartment has The refrigerant vapor passage is connected to the outside to determine that the first steam dividing chamber has a refrigerant vapor passage communicating with the second condenser, and the second condenser and the refrigerant liquid pipeline are connected to the second evaporator via the first refrigerant liquid pump. The second absorption-generator has a refrigerant vapor passage communicating with the outside to determine that the second evaporator has a refrigerant vapor passage communicating with the second absorption-generator, and the absorption-vaporizer has a refrigerant vapor passage connected to the outside. a coolant vapor channel for the first evaporator is connected to the absorption-evaporator The absorber has a refrigerant vapor passage and communicates with the outside to determine that the first evaporator has a refrigerant vapor passage communicating with the absorber, and the external refrigerant liquid pipeline is connected to the absorption-evaporator to absorb the evaporator and the refrigerant. The steam passage is connected to the first absorption-generator to determine that the first evaporator has a refrigerant liquid pipeline connected to the absorption-evaporator through the second refrigerant liquid pump, the absorption-vaporizer and the refrigerant vapor passage and the first absorption - the generator is connected, or is determined to be the first condenser having a refrigerant liquid line connected to the absorption-evaporator via the second throttle valve, the absorption-evaporator and then the refrigerant vapor channel is in communication with the first absorption-generator, The first condenser further has a heated medium line communicating with the outside, and the second condenser and the cooling medium line are in communication with the outside, and the first evaporator and the second evaporator further have a residual heat medium line respectively communicating with the outside to form Single-stage single-effect regenerative third-class absorption heat pump; wherein: 1 optionally adding a third throttle valve, the first evaporator increases the refrigerant liquid pipeline to communicate with the second evaporator via the third throttle valve, and then The second condenser has a refrigerant liquid line A first refrigerant pump in communication with the second evaporator changes The specification is that the second condenser has a refrigerant liquid pipeline connected to the first evaporator via the first refrigerant liquid pump; 2 when there is no second evaporator, the second condenser has a refrigerant liquid pipeline passing the first coolant liquid The pump is connected to the second evaporator to be changed to the second condenser. The refrigerant liquid pipeline is connected to the first evaporator via the first refrigerant liquid pump, and the first evaporator increases the refrigerant vapor passage to communicate with the second absorption generator. .

 9. A regenerative third type absorption heat pump, in the regenerative absorption-generation system in which the second absorption-generator has a medium to be heated and communicated with the outside, the first condenser is added a second condenser, a first evaporator, a second evaporator, a third evaporator, a first throttle valve, a first refrigerant liquid pump, a second throttle valve, a third throttle valve, and a second refrigerant The liquid pump or the fourth throttle valve connects the generator refrigerant vapor passage to the outside to determine that the generator has a refrigerant vapor passage communicating with the first condenser, and the first condenser and the refrigerant liquid pipeline are first The throttle valve is in communication with the second evaporator, the second evaporator and the refrigerant liquid pipeline are in communication with the first evaporator via the third throttle valve, and the first evaporator and the refrigerant liquid pipeline are connected to the second throttle The valve is in communication with the third evaporator, and the refrigerant passage of the first steam distribution chamber is communicated with the outside to determine that the first steam distribution chamber has a refrigerant vapor passage communicating with the second condenser, and the second condenser is further provided with a refrigerant liquid. The pipeline is connected to the second evaporator via the first refrigerant liquid pump, and the second absorption-generator has a refrigerant The communication between the steam passage and the outside is determined to be that the second evaporator has a refrigerant vapor passage communicating with the second absorption generator, and the absorption-vaporizer refrigerant vapor passage is communicated with the outside to determine that the third evaporator has a refrigerant vapor passage and The absorption-evaporator is connected, and the refrigerant vapor passage of the absorber is connected to the outside to determine that the first evaporator has a refrigerant vapor passage communicating with the absorber, and the external refrigerant liquid pipeline is connected to the absorption-evaporator and absorbed. The evaporator further has a refrigerant vapor passage connected to the first absorption-generator to determine that the first evaporator or the second evaporator has a refrigerant liquid pipeline connected to the absorption-evaporator through the second refrigerant liquid pump, and then absorbs-evaporates. The refrigerant vapor passage is connected to the first absorption-generator, or is determined to be the first condenser, and the refrigerant liquid pipeline is connected to the absorption-evaporator through the fourth throttle valve, and then the absorption-evaporator is further cooled. The steam passage is in communication with the first absorption generator, the first condenser further has a heated medium line communicating with the outside, and the second condenser and the cooling medium conduit are in communication with the outside, the first evaporator, the second evaporator, and Third steaming The generator also has a residual heat medium pipeline connected to the outside to form a single-stage single-effect regenerative third-type absorption heat pump; wherein: 1 may select the first condenser to have a refrigerant liquid pipeline through the first throttle valve Communicating with the second evaporator, the second evaporator and the refrigerant liquid pipeline are connected to the first evaporator through the third section, and the first condenser has a refrigerant liquid pipeline through the first throttle valve and the first An evaporator is connected, the first evaporator or the third evaporator has a refrigerant liquid pipeline connected to the second evaporator via the third throttle valve, and the second condenser has a refrigerant liquid pipeline passing through the first coolant liquid The pump is connected to the second evaporator to be changed to a second condenser. The refrigerant liquid line is connected to the second evaporator or the first evaporator via the first refrigerant liquid pump; 2 when there is no second evaporator, the second condenser The refrigerant liquid pipeline is connected to the second evaporator through the first refrigerant liquid pump to be changed to the second condenser, and the refrigerant liquid pipeline is connected to the first evaporator via the first refrigerant liquid pump, and the first condenser has The refrigerant liquid pipeline communicates with the second evaporator via the first throttle valve, and the second evaporator has a refrigerant liquid pipeline through the third section Wide communication with the first evaporator is changed to a first condenser with a refrigerant liquid of the first throttle valve communicates with the first conduit through the evaporator, the first evaporator increase refrigerant vapor passage and the second absorbing - generator in communication.

10. The regenerative third type absorption heat pump is a regenerative absorption-generation system in which the second absorption-generator is connected to the outside without the heated medium line, and the first condenser is added. a second condenser, a first evaporator, a second evaporator, a third evaporator, a first throttle valve, a first refrigerant liquid pump, a second throttle valve, a second refrigerant liquid pump, or a third section a flow valve, the generator has a refrigerant vapor passage connected to the outside to determine that the generator has a refrigerant vapor passage communicating with the first condenser, and the first condenser has a refrigerant liquid pipeline passing through the first throttle valve and the first The evaporator is connected, the first evaporator and the refrigerant liquid pipeline are connected to the third evaporator via the second throttle valve, and the refrigerant passage of the first steam distribution chamber is connected to the outside to determine that the first steam compartment has The refrigerant vapor passage is in communication with the second condenser, the second condenser and the refrigerant liquid pipeline are connected to the second evaporator via the first refrigerant liquid pump, and the second absorption generator has a refrigerant vapor passage and the outside The connection is determined to be that the second evaporator has a refrigerant vapor passage communicating with the second absorption-generator, The evaporator-vaporizer has a refrigerant vapor passage communicating with the outside to determine that the third evaporator has a refrigerant vapor passage communicating with the absorption-evaporator, and the absorber has a refrigerant vapor passage communicating with the outside to determine that the first evaporator has a refrigerant. The steam passage is in communication with the absorber, and the external refrigerant liquid line is connected to the absorption-evaporator, and the absorption-evaporator and the refrigerant vapor passage are connected to the first absorption-generator to determine that the first evaporator has a refrigerant liquid. The pipeline is connected to the absorption-evaporator through the second refrigerant liquid pump, and then the absorption-evaporator is further connected to the first absorption-generator through the refrigerant vapor passage, or is determined to be the first condenser having the refrigerant liquid pipeline. The three throttle valve is connected to the absorption-evaporator and the absorption-evaporator has a refrigerant vapor channel and a first absorption-generator The specification is connected, the first condenser has a heated medium line communicating with the outside, the second condenser and the cooling medium line are in communication with the outside, and the first evaporator, the second evaporator and the third evaporator respectively have residual heat The medium pipeline communicates with the outside to form a single-stage single-effect regenerative third-class absorption heat pump; wherein: 1 may choose to increase the fourth section of the flow, and the first evaporator or the third evaporator may increase the refrigerant liquid pipeline. The fourth throttle valve is in communication with the second evaporator, and the second condenser has a refrigerant liquid pipeline connected to the second evaporator via the first refrigerant liquid pump and the second evaporator has a coolant liquid pipeline The first refrigerant liquid pump is in communication with the first evaporator; 2 when there is no second evaporator, the second condenser has a refrigerant liquid line connected to the second evaporator via the first refrigerant liquid pump to be changed to the second condenser The refrigerant liquid pipeline is connected to the first evaporator via the first refrigerant liquid pump, and the first evaporator increases the refrigerant vapor passage to communicate with the second absorption generator.

 11. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 5-6, adding new generators, adding new throttle valves and adding solution heat exchange. The first solution pump is provided with a dilute solution pipeline connected to the newly added generator through the new solution heat exchanger, and the new generator and the concentrated solution pipeline are connected to the second absorption-generator via the newly added solution heat exchanger. , the generator has a refrigerant vapor channel and the first condenser is connected to adjust the generator to have a refrigerant vapor channel and the new generator is connected, the new generator is added, and then the refrigerant liquid pipeline is added with a new throttle valve and the first A condenser is connected - the refrigerant vapor released by the generator is used as a driving heat medium for the newly added generator, and a new generator and a refrigerant vapor passage are connected to the first condenser to form a single-stage parallel double-effect regenerative type. Three types of absorption heat pumps.

 12. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 7-10, adding new generators, adding new throttle valves and adding solution heat exchange. The first solution pump is provided with a dilute solution pipeline connected to the newly added generator through the new solution heat exchanger, and the new generator and the concentrated solution pipeline are added to the generator through the first solution after the new solution heat exchanger The concentrated solution line after the heat exchanger merges, and then communicates with the first steam dividing chamber through the second absorption-generator, and connects the refrigerant vapor channel of the generator with the first condenser to adjust the generator to have a refrigerant vapor channel After the new generator is connected, the new generator is added, and the refrigerant liquid pipeline is connected to the first condenser via the new throttle valve. The refrigerant vapor released by the generator is used as the driving heat medium for the new generator. The generator and the refrigerant vapor passage are connected to the first condenser to form a single-stage parallel double-effect regenerative third-stage absorption heat pump.

 13. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 5-6, adding new generators, adding new throttle valves and adding solution heat exchange. , the generator has a concentrated solution pipeline connected to the second absorption-generator through the first solution heat exchanger to adjust the generator to have a concentrated solution pipeline connected to the newly added generator through the new solution heat exchanger, newly added The generator further has a concentrated solution pipeline connected to the second absorption-generator via the first solution heat exchanger, and the second absorption-generator has a dilute solution pipeline connected to the generator via the first solution heat exchanger to be adjusted to The second absorption-generator has a dilute solution pipeline connected to the generator via the first solution heat exchanger and the new solution heat exchanger, and the generator has a refrigerant vapor passage connected to the first condenser to adjust the generator to have a refrigerant After the steam passage is connected with the newly added generator, a new generator is added, and the refrigerant liquid pipeline is connected to the first condenser via a new throttle valve - the refrigerant vapor released by the generator is used as a driving heat medium for the newly added generator. , new generators and refrigerant vapor channels and A condenser is connected to form a single-stage series double-effect regenerative third-class absorption heat pump.

 14. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 7-10, adding new generators, adding new throttle valves and adding solution heat exchange. The generator has a concentrated solution pipeline connected to the first split heat exchanger via the first solution heat exchanger and the second absorption generator, and the generator has a concentrated solution pipeline through the newly added solution heat exchanger and newly added The generator is connected, the new generator and the concentrated solution pipeline are connected to the first steam separation chamber through the first solution heat exchanger and the second absorption generator, and the second absorption generator has a dilute solution pipeline. A solution heat exchanger is connected to the generator to be adjusted to a second absorption-generator having a dilute solution line connected to the generator via the first solution heat exchanger and the new solution heat exchanger, and the generator has a refrigerant vapor channel and The first condenser is connected to adjust the generator to have a refrigerant vapor channel connected with the newly added generator, and then the new generator is connected, and the refrigerant liquid pipeline is connected to the first condenser via the newly added throttle valve - the generator releases Coolant steam is used as the driving heat medium for the new generator. There refrigerant vapor passage is in communication with the first condenser connected in series to form a single-stage double-effect heat recovery third type absorption heat pump.

15. The regenerative third type absorption heat pump is the regenerative third type absorption heat pump according to Item 13-14, wherein the second absorption-generator has a dilute solution line through the first solution pump , the first solution heat exchanger and the new solution heat exchanger occur Description

The device is connected to the second absorption-generator, and the dilute solution line is directly connected to the newly added generator through the first solution pump and the first solution heat exchanger, and is then connected to the generator via the new solution heat exchanger. Form a single-stage string and double-effect regenerative third-class absorption heat pump.

 16. The regenerative third type absorption heat pump is a new type of regenerative third type absorption heat pump according to items 5-6, adding new generators, adding new throttle valves, and adding new solution heat exchange. And a new solution pump, the second absorption-generator has a dilute solution line connected to the first solution pump and the first solution heat exchanger and the generator to adjust to a second absorption-generator with a dilute solution line A solution pump and a first solution heat exchanger are connected to the newly added generator, and the new generator and the concentrated solution pipeline are connected to the generator via the new solution pump and the new solution heat exchanger, and the generator has a concentrated solution. The pipeline is connected to the second absorption-generator via the first solution heat exchanger to adjust the generator to have a concentrated solution pipeline connected to the second absorption-generator via the new solution heat exchanger and the first solution heat exchanger, The generator has a refrigerant vapor passage communicating with the first condenser to adjust the generator to have a refrigerant vapor passage connected to the newly added generator, and then adding a new generator to the refrigerant liquid pipeline via the newly added throttle valve and the first condensation Connected - the refrigerant vapor released by the generator is added Driver's heat medium, as well as the new refrigerant vapor passage in communication with the first generator, the condenser, connected in series to form a single-stage double-effect heat recovery third type absorption heat pump.

 17. The regenerative third type absorption heat pump is a new type of regenerative third type absorption heat pump according to items 7-10, adding new generators, adding new throttle valves, and adding solution heat exchange. And a new solution pump, the second absorption-generator has a dilute solution line connected to the first solution pump and the first solution heat exchanger and the generator to adjust to a second absorption-generator with a dilute solution line A solution pump and a first solution heat exchanger are connected to the newly added generator, and the new generator and the concentrated solution pipeline are connected to the generator via the new solution pump and the new solution heat exchanger, and the generator has a concentrated solution. The pipeline is connected to the first steam separator through the first solution heat exchanger and the second absorption generator to adjust the generator to have a concentrated solution pipeline through the new solution heat exchanger, the first solution heat exchanger and the second absorption - the generator is in communication with the first steam dividing chamber, and the generator has a refrigerant vapor passage communicating with the first condenser to adjust the generator to have a refrigerant vapor passage and the new generator is connected, and the new generator is further provided with a refrigerant liquid. The pipeline is connected to the first condenser via a new throttle valve - the generator Discharge of refrigerant vapor as heat medium drive the new generator, as well as the new refrigerant vapor passage in communication with the first generator, the condenser, connected in series to form a single-stage double-effect heat recovery third type absorption heat pump.

 18. The regenerative third type absorption heat pump is the regenerative third type absorption heat pump according to Item 16-17, wherein the second absorption-generator has a dilute solution line through the first solution pump And communicating with the first solution heat exchanger and the newly added generator to adjust to a second absorption-generator having a dilute solution line connected to the newly added generator and the generator through the first solution pump and the first solution heat exchanger, respectively A single-stage series-parallel double-effect regenerative third-class absorption heat pump is formed.

 19. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 5-6, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger and the addition of the second solution heat exchanger, and the first solution pump adding the dilute solution pipeline respectively by adding the first solution heat exchange The first generator is connected to the newly added first generator and the second solution heat exchanger is connected with the newly added second generator, and the first generator and the concentrated solution pipeline are added through the newly added first solution heat exchanger. The second absorption-generator is connected, the second generator and the concentrated solution pipeline are connected to the second absorption-generator via the newly added second solution heat exchanger, and the generator has a refrigerant vapor passage and a first condensation The device is connected to adjust the generator to have a refrigerant vapor channel connected with the newly added first generator, and then the first generator is added, and then the refrigerant liquid pipeline is connected to the first condenser through the addition of the first throttle valve - occurs The refrigerant vapor generated by the device is used as the driving heat medium for adding the first generator, adding the first hair The refrigerant flow channel is connected with the newly added second generator, and the second generator is added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve - the first occurrence occurs. The refrigerant vapor generated by the device is used as the driving heat medium for adding the second generator. The second generator and the refrigerant vapor channel are connected to the first condenser to form a single-stage parallel three-effect regenerative third-class absorption. Heat pump.

20. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 7-10, adding a new first generator, adding a second generator, adding The first section is wide, the second throttle valve is added, the first solution heat exchanger is added, and the second solution heat exchanger is added. The first solution pump is added with the dilute solution pipeline, and the first solution heat exchange is newly added. Connected with the newly added first generator and connected to the newly added second generator by adding the second solution heat exchanger, adding the first generator having the concentrated solution pipeline after adding the first solution heat exchanger and Add a second generator with a concentrated solution line to add a second solution After the heat exchanger, the generator is merged with the concentrated solution pipeline after the first solution heat exchanger, and then connected to the first steam distribution chamber via the second absorption generator, and the generator has a refrigerant vapor passage and the first The condenser is connected to adjust the generator to have a refrigerant vapor channel connected with the newly added first generator, and then the first generator is added, and then the refrigerant liquid pipeline is connected to the first condenser through the addition of the first throttle valve - The refrigerant vapor generated by the generator is used as the driving heat medium for adding the first generator, and the first generator and the refrigerant vapor channel are connected with the newly added second generator to add a second generator and then a refrigerant. The liquid pipeline is connected to the first condenser via a new second throttle valve - the refrigerant vapor generated by the first generator is added as the driving heat medium for the second generator, and the second generator is added. The refrigerant vapor passage is in communication with the first condenser to form a single-stage parallel three-effect regenerative third-stage absorption heat pump.

 21. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 5-6, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger and the addition of the second solution heat exchanger, the generator has the concentrated solution pipeline through the first solution heat exchanger and the second The absorption-generator connection is adjusted so that the generator has a concentrated solution pipeline connected to the newly added first generator via the first solution heat exchanger, and the first generator and the concentrated solution pipeline are added with the first solution heat exchange. The second generator is connected to the newly added second generator, and the second generator and the concentrated solution pipeline are connected to the second absorption generator via the newly added second solution heat exchanger, and the second absorption generator has a dilute solution. The pipeline is connected to the generator through the first solution pump and the first solution heat exchanger to adjust to a second absorption-generator having a dilute solution pipeline through the first solution pump, adding a second solution heat exchanger, adding a first The solution heat exchanger and the first solution heat exchanger are connected to the generator, and the generator has The agent steam passage is connected with the first condenser to adjust the generator to have a refrigerant vapor passage connected with the newly added first generator, and then the first generator is added, and then the refrigerant liquid pipeline is added with the first throttle valve and the first A condenser is connected - the refrigerant vapor generated by the generator is used as the driving heat medium for adding the first generator, and the first generator and the refrigerant vapor channel are connected with the newly added second generator to add a second The generator further has a refrigerant liquid pipeline connected to the first condenser via a new second throttle valve - adding the refrigerant vapor generated by the first generator as a driving heat medium for adding the second generator, adding The second generator also has a refrigerant vapor passage communicating with the first condenser to form a single-stage series three-effect regenerative third type absorption heat pump.

 22. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 7-10, adding a new first generator, adding a second generator, adding a first throttle valve, a second throttle valve, a first solution heat exchanger and a second solution heat exchanger are added, the generator has a concentrated solution pipeline through the first solution heat exchanger and the second The absorption-generator is connected to the first steam separation chamber to adjust the generator to have a concentrated solution pipeline connected to the newly added first generator through the first solution heat exchanger, and the first generator and the concentrated solution pipeline are newly added. The first solution heat exchanger is in communication with the newly added second generator, and the second addition generator and the concentrated solution line are connected to the first distribution chamber via the newly added second solution heat exchanger and the second absorption generator. a second absorption-generator having a dilute solution line connected to the first solution pump and the first solution heat exchanger and the generator to be adjusted to a second absorption-generator having a dilute solution line through the first solution pump, newly added a second solution heat exchanger, a new first solution heat exchanger, and a first solution heat exchanger The device is connected, the generator has a refrigerant vapor channel connected to the first condenser, and the generator has a refrigerant vapor channel connected with the newly added first generator, and then the first generator is added and then the refrigerant liquid pipeline is replaced by a new one. The first throttle valve is connected to the first condenser--the refrigerant vapor generated by the generator is used as the driving heat medium for adding the first generator, and the first generator is added with the refrigerant vapor channel and the second is added. After the generator is connected, a second generator is added, and then the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve - the refrigerant coolant generated by the first generator is added as the second new generation. The driving heat medium of the device, the second generator and the refrigerant vapor channel are connected with the first condenser to form a single-stage series three-effect regenerative third type absorption heat pump.

23. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in item 5-6, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger, the addition of the second solution heat exchanger, the addition of the first solution pump and the addition of the second solution pump, the second absorption - the generator has a dilute solution line connected to the generator via the first solution pump and the first solution heat exchanger to adjust to a second absorption - the generator has a dilute solution line through the first solution pump and the first solution heat exchanger A second generator connection is added, a second generator and a concentrated solution line are added, and a second solution pump is added and a second solution heat exchanger is added to connect with the newly added first generator. The concentrated solution pipeline is connected to the generator via the newly added first solution pump and the newly added first solution heat exchanger, and the generator has a concentrated solution. The pipeline is connected to the second absorption-generator through the first solution heat exchanger to adjust the generator to have a concentrated solution pipeline, the first solution heat exchanger is added, the second solution heat exchanger is added, and the first solution heat exchanger is exchanged. The device is connected to the second absorption-generator, and the generator has a refrigerant vapor channel connected to the first condenser to adjust the generator to have a refrigerant vapor channel connected with the newly added first generator, and then the first generator is added. The refrigerant liquid pipeline is connected to the first condenser by adding a first throttle valve - the refrigerant vapor generated by the generator is used as a driving heat medium for adding the first generator, and the first generator and the refrigerant are newly added. The steam passage is connected with the newly added second generator, and the second generator is newly added, and the refrigerant liquid pipeline is connected with the first condenser through the addition of the second throttle valve - the refrigerant generated by the first generator is newly added. As the driving heat medium of the newly added second generator, steam is added to the second generator and the refrigerant vapor passage is connected with the first condenser to form a single-stage series three-effect regenerative third type absorption heat pump.

 24. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 7-10, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger, the addition of the second solution heat exchanger, the addition of the first solution pump and the addition of the second solution pump, the second absorption - the generator has a dilute solution line through the first solution pump and the first solution heat exchanger is connected to the generator to adjust to a second absorption - the generator has a dilute solution line through the first solution pump and the first solution heat exchanger Connected with the newly added second generator, the new second generator and the concentrated solution pipeline are connected with the newly added first generator by adding the second solution pump and the newly added second solution heat exchanger, adding the first The generator also has a concentrated solution pipeline connected to the generator via the newly added first solution pump and the newly added first solution heat exchanger, and the generator has a concentrated solution pipeline through the first solution heat exchanger and the second absorption-occurrence The device is connected to the first steam compartment of the book to adjust the generator to have a concentrated solution pipeline. The converter, the newly added second solution heat exchanger, the first solution heat exchanger and the second absorption-generator are in communication with the first steam dividing chamber, and the generator refrigerant vapor passage is connected to the first condenser to be adjusted to occur The refrigerant coolant channel is connected with the newly added first generator, and the first generator is added, and then the refrigerant liquid pipeline is connected with the first condenser through the addition of the first throttle valve - the refrigerant generated by the generator Steam is used as the driving heat medium for adding the first generator. The first generator is added, and the refrigerant vapor channel is connected with the newly added second generator. The second generator is added and the refrigerant liquid pipeline is added. The second throttle valve is in communication with the first condenser - the refrigerant coolant generated by the first generator is added as the driving heat medium for adding the second generator, and the second generator is further provided with the refrigerant vapor passage and the second A condenser is connected to form a single-stage series three-effect regenerative third-class absorption heat pump.

 25. The regenerative third type absorption heat pump is a heat-increasing type III absorption heat pump according to item 5, adding a new solution heat exchanger, adding an absorption-evaporator and adding a new refrigerant. The liquid pump adjusts the absorption-evaporator with a dilute solution line through the third solution pump to the first absorption-generator to absorb-the evaporator has a dilute solution line through the new solution heat exchanger and the new absorption-evaporation Connected, the new absorption-evaporator and the dilute solution line are connected to the first absorption-generator via the third solution pump and the new solution heat exchanger, respectively, and the first evaporator has a refrigerant vapor channel separately and absorbed - The evaporator and the absorber are connected to each other such that the first evaporator has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the first evaporator or the second condenser is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump and the new After the absorption-evaporator is connected, a new absorption-evaporator is added, and then a refrigerant vapor channel is respectively connected with the absorption-evaporator and the absorber to form a single generator which supplies the refrigerant vapor to the absorber by the new absorption-evaporator. Class regenerative third type absorption heat pump.

 26. The regenerative third type absorption heat pump is a new type of regenerative liquid pump or a new throttle valve or a new solution in the regenerative third type absorption heat pump described in items 7-8. Heat exchanger and new absorption-evaporator, the absorption-evaporator has a dilute solution line connected to the first absorption-generator through the third solution pump to adjust to absorption-the evaporator has a dilute solution line through the new solution heat The exchanger is connected to the new absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the first absorption-generator via the third solution pump and the new solution heat exchanger, and the first evaporator has The refrigerant vapor passages are respectively connected with the absorption-evaporator and the absorber, and the first evaporator has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the first evaporator adds a refrigerant liquid pipeline through the newly added refrigerant liquid. After the pump is connected with the new absorption-evaporator, the absorption-evaporator is added, and then the refrigerant vapor channel is connected to the absorption-evaporator and the absorber respectively, or the first condenser is added with the refrigerant liquid pipeline through the new throttle valve. Adding an absorption-evaporator to the new absorption-evaporator Hood respectively Absorption - communicating evaporator and absorber, formed by a new absorber - evaporator to provide refrigerant vapor to the absorber single generator third two recuperative heat absorption heat pump.

27. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in item 5. Increasing solution heat exchanger, new solution pump, new absorption-evaporator and new refrigerant liquid pump, connecting the absorber with dilute solution line and absorption-evaporator to adjust to the absorber with dilute solution line The increasing solution heat exchanger is connected to the newly added absorption-evaporator, and the new absorption-evaporator and the dilute solution pipeline are connected to the absorption-evaporator via the new solution pump and the new solution heat exchanger, and the first evaporator is connected. The refrigerant vapor passages are respectively connected with the absorption-evaporator and the absorber, and the first evaporator has a refrigerant vapor passage communicating with the new absorption-evaporator, and the first evaporator or the second condenser is provided with a refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the new absorption-evaporator, the absorption-evaporator is added and the refrigerant vapor channel is connected to the absorption-evaporator and the absorber respectively, forming a new absorption-evaporator to the absorber. A single-generator two-stage regenerative third-stage absorption heat pump that provides refrigerant vapor.

 28. The regenerative third type absorption heat pump is a new type of refrigerant liquid pump or a new throttle valve or a new solution added to the regenerative third type absorption heat pump described in items 7-8. Heat exchanger, new solution pump and new absorption-evaporator, connect the absorber with dilute solution line and absorption-evaporator to adjust the absorber to dilute solution line through new solution heat exchanger and add absorption - The evaporator is connected, the new absorption-evaporator and the dilute solution pipeline are connected to the absorption-evaporator through the new solution pump and the new solution heat exchanger, and the first evaporator has the refrigerant vapor passage and absorption respectively. - The evaporator and the absorber are connected to each other so that the first evaporator has a refrigerant vapor passage communicating with the newly added absorption-evaporator, and the first evaporator is provided with a refrigerant liquid pipeline via a newly added refrigerant liquid pump and a new absorption-evaporation After the device is connected, the absorption-evaporator is added, and then the refrigerant vapor channel is respectively connected with the absorption-evaporator and the absorber, or the first condenser is added with the refrigerant liquid pipeline through the newly added throttle valve and the newly added absorption-evaporator. After the connection, the absorption-evaporator is added and the refrigerant vapor channel is separately absorbed and absorbed. Hair and absorber communication, a new book is formed absorber - evaporator to provide refrigerant vapor to the absorber single generator third two recuperative heat absorption heat pump.

 29. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to item 5, adding a new solution heat exchanger, adding an absorption-evaporator, and adding a new refrigerant. The liquid pump and the newly added solution pump adjust the second solution compartment to have a concentrated solution line and the absorber, and adjust to a second distribution chamber, a concentrated solution line, a new solution pump, and a new solution heat exchanger and absorber. Connected, the absorber has a dilute solution line connected to the absorption-evaporator to adjust the absorber to a dilute solution line. The new solution heat exchanger is connected to the new absorption-evaporator, and the new absorption-evaporator is thin. The solution line is connected to the absorption-evaporator, and the first evaporator has a refrigerant vapor channel connected to the absorber to be adjusted to be a first evaporator having a refrigerant vapor channel connected to the new absorption-evaporator, the first evaporator or the first The second condenser is provided with a refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the new absorption-evaporator, a new absorption-evaporator is connected, and then the refrigerant vapor passage is connected with the absorber to form a new absorption-evaporator. Single generator two-stage heat recovery that supplies refrigerant vapor to the absorber The third type of absorption heat pump.

 30. The regenerative third type absorption heat pump is a new type of refrigerating liquid pump or a new throttle valve, adding new solution heat in the regenerative third type absorption heat pump described in Item 78. The exchanger, the new absorption-evaporator and the new solution pump, the second distribution chamber has a concentrated solution line connected to the absorber, and the second distribution chamber has a concentrated solution line through the new solution pump and newly added The solution heat exchanger is in communication with the absorber, and the absorber has a dilute solution line connected to the absorption-evaporator to adjust the absorber to a dilute solution line, and the new solution heat exchanger is connected with the new absorption-evaporator. The absorption-evaporator further has a dilute solution line connected to the absorption-evaporator, and the first evaporator has a refrigerant vapor channel connected to the absorber to adjust the first evaporator to have a refrigerant vapor channel connected to the new absorption-evaporator. The first evaporator adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump and connects with the new absorption-evaporator, and then adds an absorption-evaporator, and then the refrigerant vapor channel communicates with the absorber, or the first condenser is added. The refrigerant liquid line is connected to the new absorption-evaporator via a new throttle valve. A new absorption-evaporator is then added to the refrigerant vapor passage to communicate with the absorber to form a single-stage two-stage regenerative third-stage absorption heat pump that supplies refrigerant vapor to the absorber by a new absorption-evaporator.

31. The regenerative third type absorption heat pump is a new type of refrigerant liquid pump, a new solution heat exchanger and a new absorber in the regenerative third type absorption heat pump described in item 5. , the absorption-evaporator has a dilute solution pipeline connected to the first absorption-generator through the third solution pump and adjusted to absorb-the evaporator has a dilute solution pipeline through the third solution pump and the new solution heat exchanger and newly added The absorber is connected, the new absorber and the dilute solution pipeline are connected to the first absorption-generator via the new solution heat exchanger, and the absorber is connected to the external medium by the heating medium pipeline to adjust to the first evaporator or the first The second condenser is provided with a refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the absorber, the absorber is newly added, and then the refrigerant vapor passage is connected with the newly added absorber, and the newly added absorber and the heated medium pipeline are connected. Externally connected, a single-stage two-stage regenerative third-stage absorption heat pump that provides refrigerant vapor to the newly added absorber from the absorber. 32. Regenerative third type absorption heat pump, in the regenerative third type absorption heat pump described in items 7-8, adding a new refrigerant liquid pump or adding a new throttle valve, adding a new solution The heat exchanger and the newly added absorber, the absorption-evaporator having a dilute solution line is connected to the first absorption-generator through the third solution pump to be adjusted to absorb-the evaporator has a dilute solution line through the third solution pump and the new The increasing solution heat exchanger is connected with the newly added absorber, and the newly added absorber and the dilute solution pipeline are connected to the first absorption-generator via the newly added solution heat exchanger, and the absorber has the heated medium pipeline connected to the outside. Adjusting to add the coolant liquid pipeline to the first evaporator. After the new refrigerant liquid pump is connected with the absorber, the absorber is added, and then the refrigerant vapor channel is connected with the newly added absorber, or adjusted to be the first condenser. The agent liquid pipeline is connected with the absorber through the newly added throttle valve, and then the absorber is added, and the refrigerant vapor passage is connected with the newly added absorber. The newly added absorber and the heated medium pipeline communicate with the outside to form an absorption. Single-generator two-stage regenerative system that supplies refrigerant vapor to the newly added absorber Three absorption heat pump.

 33. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to item 5, adding a new refrigerant liquid pump or a new throttle valve, and adding a solution heat exchange. And a new absorber, the generator has a concentrated solution pipeline connected to the second absorption-generator through the first solution heat exchanger, and is adjusted to have a concentrated solution pipeline through the first solution heat exchanger and newly added The absorber is connected, the new absorber and the dilute solution pipeline are connected to the second absorption generator via the new solution heat exchanger, and the second absorption generator has a dilute solution pipeline through the first solution pump and the first solution. The heat exchanger is connected to the generator to be adjusted to a second absorption-generator having a dilute solution line connected to the generator via the first solution pump, the new solution heat exchanger and the first solution heat exchanger, and the absorber is heated The medium pipe is connected to the outside to adjust to the book. The second evaporator is provided with a refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the absorber, the absorber has a refrigerant vapor channel connected to the newly added absorber, or adjusted to the first A new refrigerant is added to the condenser to increase the throttling After being connected with the absorber, the absorber further has a refrigerant vapor passage communicating with the newly added absorber, and the newly added absorber and the heated medium pipeline communicate with the outside to form a single sheet for supplying the refrigerant vapor to the newly added absorber by the absorber. Generator two-stage regenerative third type absorption heat pump; wherein, when there is no second evaporator, the second evaporator has a refrigerant liquid pipeline connected to the absorber through the newly added refrigerant liquid pump, and then the absorber is cold The agent steam passage is connected with the newly added absorber to be changed to the first evaporator. The refrigerant liquid pipeline is connected to the absorber through the newly added refrigerant liquid pump, and then the absorber has a refrigerant vapor passage communicating with the newly added absorber.

 34. The regenerative third type absorption heat pump is a new type of refrigerating liquid pump or a new throttle valve or a new solution in the regenerative third type absorption heat pump described in items 7-8. a heat exchanger and a new absorber, the generator has a concentrated solution pipeline connected to the first split heat exchanger via the first solution heat exchanger and the second absorption generator, and the generator has a concentrated solution pipeline through the first The solution heat exchanger is connected to the newly added absorber, and the new absorber and the dilute solution pipeline are connected to the first steam split chamber via the new solution heat exchanger and the second absorption generator, and the second absorption generator The dilute solution pipeline is connected to the generator through the first solution pump and the first solution heat exchanger to adjust to a second absorption-generator having a dilute solution pipeline through the first solution pump, the new solution heat exchanger and the first solution The heat exchanger is connected with the generator, and the absorber has a heating medium pipeline connected to the outside to adjust to the first evaporator. The refrigerant liquid pipeline is connected to the absorber through the newly added refrigerant liquid pump, and the absorber has a refrigerant. The steam passage is connected to the newly added absorber, or is adjusted to have a refrigerant in the first condenser After the pipeline is connected with the absorber through the newly added throttle valve, the absorber has a refrigerant vapor passage and communicates with the newly added absorber, and the newly added absorber and the heated medium pipeline communicate with the outside, forming an increase from the absorber. The absorber provides a single generator two-stage regenerative third type absorption heat pump with refrigerant vapor.

35. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to item 5, adding a new refrigerant liquid pump or a new throttle valve, and adding a solution heat exchange. , a new absorber and a new solution pump, the generator has a concentrated solution pipeline connected to the second absorption-generator through the first solution heat exchanger to adjust the generator to have a concentrated solution pipeline through the first solution heat exchange And the new solution heat exchanger is connected to the second absorption-generator, and the second absorption-generator has a dilute solution line connected to the first solution pump and the first solution heat exchanger and the generator to adjust to a second absorption - The generator has a dilute solution line connected to the newly added absorber via the first solution pump and the new solution heat exchanger, and the new absorber and the dilute solution line are connected to the first solution heat exchanger by the new solution pump and the dilute solution line The generator is connected, and the absorber has a heating medium pipeline connected to the outside to adjust to a second evaporator to add a refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the absorber, the absorber has a refrigerant vapor channel and a new one. The absorber is connected or adjusted to add a refrigerant liquid to the first condenser After the new throttle valve is connected with the absorber, the absorber has a refrigerant vapor passage connected with the newly added absorber, and the newly added absorber and the heated medium pipeline communicate with the outside to form an absorption from the absorber. a single-stage two-stage regenerative third-stage absorption heat pump that supplies refrigerant vapor; wherein, when there is no second evaporator, In the second evaporator of the evaporator, the refrigerant liquid pipeline is connected to the absorber through the newly added refrigerant liquid pump, and then the absorber is connected with the refrigerant vapor passage and the newly added absorber, and the first evaporator has a refrigerant liquid pipeline. After the refrigerant liquid pump is connected with the absorber, the absorber further has a refrigerant vapor passage communicating with the newly added absorber.

 36. The regenerative third type absorption heat pump is a new type of refrigerant liquid pump or a new throttle valve or a new solution added in the regenerative third type absorption heat pump described in items 7-8. a heat exchanger, a new absorber and a new solution pump, and the concentrated solution line of the generator is connected to the first steam separation chamber through the first solution heat exchanger and the second absorption generator to adjust the generator to have a concentrated solution The pipeline is connected to the first steam separation chamber via the first solution heat exchanger, the new solution heat exchanger and the second absorption generator, and the second absorption generator has a dilute solution pipeline through the first solution pump and the first A solution heat exchanger is connected to the generator to adjust to a second absorption - the generator has a dilute solution line connected to the newly added absorber via the first solution pump and the new solution heat exchanger, and the new absorber and the dilute solution tube The new solution pump and the first solution heat exchanger are connected to the generator, and the absorber has a heating medium pipeline connected to the outside to adjust the first evaporator to have a refrigerant liquid pipeline through the newly added refrigerant liquid pump and After the absorber is connected, the absorber has a refrigerant vapor channel connected to the newly added absorber, Or adjust to the first condenser, the refrigerant liquid pipeline is connected to the absorber through the newly added throttle valve, and then the absorber has a refrigerant vapor passage to communicate with the newly added absorber, and the new absorber and the heated medium pipeline are added. In communication with the outside, a single-stage two-stage regenerative third-stage absorption heat pump that supplies refrigerant vapor to the newly added absorber is formed.

 37. The regenerative third type absorption heat pump is a new type of regenerative heat pump, a new solution heat exchanger, and a new solution pump in the regenerative third type absorption heat pump described in items 5-10. And adding a absorber, the generator has a refrigerant vapor channel and the first condenser is connected to adjust the generator to have a refrigerant vapor channel and the new absorber is connected, the new absorber and the dilute solution pipeline are added with the new solution. The pump and the new solution heat exchanger are connected to the new generator. The new generator and the concentrated solution line are connected to the newly added absorber through the new solution heat exchanger. The new generator also has a refrigerant vapor channel. It is in communication with the first condenser and has a driving heat medium pipe connected to the outside, and the newly added absorber and the heated medium pipe communicate with the outside to form a double generator which supplies the refrigerant vapor to the newly added absorber by the generator. Class regenerative third type absorption heat pump.

 38. Regenerative third type absorption heat pump, in the regenerative third type absorption heat pump described in items 5-10, adding new generator, new solution heat exchanger, new solution pump , Adding a new absorber, adding a new condenser and adding a new throttle valve, the generator adds a refrigerant vapor channel to connect with the newly added absorber, adding a new absorber and a dilute solution pipeline through a new solution pump and a new solution. The heat exchanger is connected to the newly added generator. The new generator and the concentrated solution pipeline are connected to the newly added absorber through the new solution heat exchanger. The new generator and the refrigerant vapor passage are connected to the newly added condenser. The new condenser and the refrigerant liquid pipeline are connected to the first condenser via a new throttle valve, and the new generator and the driving heat medium pipeline are connected to the outside, and the new absorber and the new condenser are added. A heated medium line is connected to the outside to form a double-generator two-stage regenerative third type absorption heat pump that supplies refrigerant vapor to the first condenser and the newly added absorber respectively.

 39. The regenerative third type absorption heat pump is a new type of regenerative heat pump added to the regenerative third type absorption heat pump described in items 5 and 7-8. The solution pump and the newly added absorber adjust the refrigerant vapor passage of the first evaporator to the absorption-evaporator and the absorber respectively to adjust the first evaporator to have a refrigerant vapor passage and communicate with the newly added absorber, and add an absorber. The dilute solution pipeline is connected to the newly added generator through the new solution pump and the new solution heat exchanger, and the new generator and the concentrated solution pipeline are connected to the newly added absorber through the new solution heat exchanger, The increase generator and the refrigerant vapor passage are respectively connected with the absorption-evaporator and the absorber, and the newly added generator also drives the heat medium pipeline to communicate with the outside, and the newly added absorber and the heated medium pipeline communicate with the outside. A two-stage two-stage regenerative third type absorption heat pump is formed which is provided with a new generator to the absorber or to the absorber and the absorption-evaporator.

 40. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to item 39, adding a new condenser and a new throttle valve, and adding a new refrigerant to the generator. The steam passage is connected with the newly added condenser, and the newly added condenser and the refrigerant liquid pipeline are connected to the first evaporator through the newly added throttle, and the newly added condenser and the heated medium pipeline communicate with the outside, forming a A new two-stage regenerative third-stage absorption heat pump with new generators for adding new condensers and absorbers or adding refrigerant vapor to new condensers, absorbers and absorption-evaporators.

41. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump in which the absorption-evaporator and the second absorption-generator are connected to the outside without a heated medium line as described in item 5. In addition, add a new coolant pump or a new throttle valve, The specification adds a new generator, a new solution heat exchanger, a new solution pump and a new absorber, and the generator has a refrigerant vapor channel connected to the first condenser to adjust the generator to have a refrigerant vapor channel and a new absorption. The device is connected, the new absorber and the dilute solution pipeline are connected to the newly added generator through the new solution pump and the new solution heat exchanger, and the new generator and the concentrated solution pipeline are added to the new solution heat exchanger. The absorber is connected, the absorber is connected to the outside by the heating medium pipeline, and the refrigerant is connected to the second evaporator. The refrigerant liquid pipeline is connected to the absorber through the newly added refrigerant liquid pump, and the absorber has a refrigerant vapor channel. Connected with the newly added absorber, or adjusted to add the refrigerant liquid pipeline to the first condenser. After the new throttle valve is connected with the absorber, the absorber is further connected with the refrigerant vapor passage and the newly added absorber. There is also a refrigerant vapor channel communicating with the first condenser and a driving heat medium pipe communicating with the outside, and the newly added absorber and the heated medium pipe are connected to the outside to form a common addition by the absorber and the generator. Absorber Double generator two-stage regenerative third type absorption heat pump for refrigerant steam; wherein, when there is no second evaporator, the second evaporator is added with a refrigerant liquid pipeline connected to the absorber through the newly added refrigerant liquid pump After the absorber is further connected with the refrigerant vapor channel and the newly added absorber, the refrigerant is added to the first evaporator to add a refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the absorber, the absorber has a refrigerant vapor channel and newly added. The absorber is connected.

 42. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump in which the absorption-evaporator is not connected to the outside by the heating medium line, and the additional refrigerant is added. Liquid pump or new throttle valve, new generator, new solution heat exchanger, new solution pump and new absorber, connect the generator refrigerant vapor passage to the first condenser to adjust the generator to The refrigerant vapor channel is connected to the newly added absorber, and the new absorber and the dilute solution pipeline are connected to the newly added generator through the new solution pump and the new solution heat exchanger, and the new generator and the concentrated solution pipeline are added. The newly added solution heat exchanger is connected with the newly added absorber, and the absorber has the heated medium pipeline connected to the outside to adjust to the first evaporator to add the refrigerant liquid pipeline. After the new refrigerant liquid pump is connected with the absorber, The absorber further has a refrigerant vapor passage connected to the newly added absorber, or is adjusted to be the first condenser. The refrigerant liquid pipeline is connected to the absorber through the newly added throttle valve, and the absorber has a refrigerant vapor passage and a new one. The absorber is connected, and the new generators are also cold. The steam passage is in communication with the first condenser and has a driving heat medium pipe connected to the outside, and the newly added absorber and the heated medium pipe communicate with the outside to form a refrigerant to be added to the newly added absorber by the absorber and the generator. Steam double generator two-stage regenerative third type absorption heat pump.

 43. The regenerative third type absorption heat pump is a new type of regenerative liquid pump, a new generator, and a new solution heat exchanger in the regenerative third type absorption heat pump described in item 5. a new solution pump and a new absorption-evaporator are provided, and the refrigerant vapor channel of the first evaporator is connected to the absorption-evaporator and the absorber, respectively, and the first evaporator has a refrigerant vapor channel and a new absorption-evaporation. The device is connected, the new absorption-evaporator and the dilute solution pipeline are connected to the newly added generator through the new solution pump and the new solution heat exchanger, and the new generator and the concentrated solution pipeline are exchanged by the new solution heat exchange. The device is connected to the new absorption-evaporator, and the first evaporator or the second condenser is provided with a refrigerant liquid pipeline. The new refrigerant liquid pump is connected with the new absorption-evaporator, and the absorption-evaporator is added and then cooled. The vapor passages of the agent are respectively connected with the absorber and the absorption-evaporator, and the newly added generator and the refrigerant vapor passage are respectively connected with the absorption-evaporator and the absorber, and the new generator and the driving heat medium pipeline are connected to the outside. Formed by new absorption-evaporator and new hair Collectively to the absorber or the absorber and the absorber together - provide an evaporator of the refrigerant vapor generator bis third two recuperative heat absorption heat pump.

44. The regenerative type III absorption heat pump is a new type of refrigerating liquid pump or a new throttle valve added in the regenerative third type absorption heat pump described in items 7-8. , a new solution heat exchanger, a new absorption-evaporator and a new solution pump, and the refrigerant vapor channel of the first evaporator is connected to the absorption-evaporator and the absorber respectively to be adjusted to a first evaporator with a refrigerant The steam channel is connected to the new absorption-evaporator, and the new absorption-evaporator and dilute solution line are connected to the new generator through the new solution pump and the new solution heat exchanger. The new generator and the concentrated solution are added. The pipeline is connected to the newly added absorption-evaporator via the newly added solution heat exchanger, and the first condenser is provided with a refrigerant liquid pipeline. After the new throttle valve is connected with the newly added absorption-evaporator, the absorption is newly added - the evaporator is further The refrigerant vapor passage is respectively connected with the absorber and the absorption-evaporator, or the first evaporator is added with a refrigerant liquid pipeline, and the new refrigerant liquid pump is connected with the new absorption-evaporator to add an absorption-evaporator. The refrigerant vapor channel is connected to the absorber and the absorption-evaporator respectively, and the new generator is also The refrigerant vapor passages are respectively connected to the absorption-evaporator and the absorber, and the newly added generator also drives the heat medium pipeline to communicate with the outside, forming a common absorption-evaporator and a new generator to the absorber or the common direction. The absorber and absorption-evaporator provide a dual generator two-stage regenerative third type absorption heat pump for refrigerant vapor. Instruction manual

 45. The regenerative type III absorption heat pump is a new type of regenerative heat pump and a new type of throttle valve in the regenerative third type absorption heat pump described in item 41. The steam passage of the agent is connected to the first condenser to adjust to a new generator having a refrigerant vapor passage communicating with the newly added condenser, and the new condenser and the refrigerant liquid pipeline are connected to the first condenser via a new throttle valve. The generator and the absorber respectively add a refrigerant vapor passage to communicate with the first condenser, and the newly added condenser and the heated medium pipeline communicate with the outside, formed by the absorber and the generator together to the first condenser and the new The absorber provides a dual generator two-stage regenerative third type absorption heat pump with refrigerant vapor.

 46. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to item 42, adding a new condenser and adding a second throttle valve, and adding a new generator The refrigerant vapor passage is connected with the first condenser to adjust the new generator to have a refrigerant vapor passage to communicate with the newly added condenser, and the new condenser and the refrigerant liquid pipeline are added with the second throttle valve and the first A condenser is connected, and the generator and the absorber respectively add a refrigerant vapor channel to communicate with the first condenser, and the newly added condenser and the heated medium pipe communicate with the outside, and the absorber and the generator are respectively combined to the first The condenser and the new absorber provide a dual generator two-stage regenerative third type absorption heat pump with refrigerant vapor.

 47. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump described in Item 1-18, adding a new condenser and adding a second throttle valve, the generator An additional refrigerant vapor channel is connected to the newly added condenser, and a new condenser and a refrigerant liquid line are connected to the first condenser via a new second throttle valve, and a new condenser and a heated medium line are added. Externally connected, a single-stage double-effect regenerative third-class absorption heat pump with a new high-temperature heating end is added.

 48. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to items 19-24, adding a new condenser and adding a third throttle valve, and adding a generator. The refrigerant vapor passage is connected to the newly added condenser, and the new condenser and the refrigerant liquid pipeline are connected to the first condenser through the addition of the third throttle valve, and the new condenser has the heated medium pipeline and the external Connected to form a single-stage three-effect regenerative third-class absorption heat pump with a new condenser as an additional high-temperature heating end.

 49. The regenerative third type absorption heat pump is a new type of regenerative heat pump in the regenerative third type absorption heat pump described in items 19-24. A generator adds a refrigerant vapor channel to communicate with the newly added condenser, and a new condenser and a refrigerant liquid line are connected to the first condenser via a new third throttle valve, and a new condenser and a heated medium are added. The pipeline communicates with the outside to form a single-stage three-effect regenerative third-type absorption heat pump with a new condenser as an additional high-temperature heating end.

 50. The regenerative third type absorption heat pump is a new type of first flow regulating valve and a second new flow regulating valve added in the regenerative third type absorption heat pump described in items 47-49. The first condenser has a heated medium pipeline connected to the outside to be adjusted to be externally connected to the first condenser by the heated medium pipeline, and the first condenser and the heated medium pipeline are respectively added with the first flow restriction. The valve is connected to the outside and is connected with the newly added condenser by the addition of the second flow regulating valve, and the newly added condenser has the heated medium pipe connected to the outside to be adjusted to be the first condenser. After the two flow throttle valve is connected with the newly added condenser, the new condenser is connected and the heated medium pipeline communicates with the outside to form an adjustable type of regenerative third type absorption heat pump.

 51. The regenerative third type absorption heat pump is a new type of regenerative third type absorption heat pump described in items 11-18, adding a second generator, adding a new absorber, and adding a new solution pump. And adding a solution heat exchanger, adding a new first generator having a refrigerant vapor passage and communicating with the first condenser to adjust to add a new first generator having a refrigerant vapor passage to communicate with the newly added absorber, adding an absorber There is also a dilute solution pipeline connected to the newly added second generator via a new solution pump and a new solution heat exchanger, and a second generator and a concentrated solution pipeline are added through the new solution heat exchanger and newly absorbed. The second generator further has a refrigerant vapor passage communicating with the first condenser and a driving heat medium conduit communicating with the outside, and the newly added absorber and the heated medium conduit are connected to the outside to form The single-stage double-effect is the first-stage two-stage regenerative third-class absorption heat pump.

 52. The regenerative third type absorption heat pump is a new type of second type throttle valve added in the regenerative third type absorption heat pump according to item 51, and the second added generator is heated. The medium pipeline is connected to the outside to adjust the generator to add a refrigerant vapor channel to the newly added second generator, and then the second generator is added, and then the refrigerant liquid pipeline is added with the second throttle valve and the first condenser. Connected - the refrigerant vapor released by the generator is used as the driving heat medium for the addition of the second generator to form a two-stage regenerative third type absorption heat pump with a single stage double effect as the first stage.

53. The regenerative third type absorption heat pump is added to the regenerative third type absorption heat pump described in items 1 to 18 Instructions added new second generator, new absorber, new solution pump, new solution heat exchanger, new condenser and new second throttle valve, new first generator added refrigerant vapor channel Connected with the newly added absorber, the new absorber and the dilute solution pipeline are connected to the newly added second generator via the new solution pump and the new solution heat exchanger, and the second generator and the concentrated solution pipeline are added. The newly added solution heat exchanger is connected with the newly added absorber, and the newly added second generator also has a refrigerant vapor passage connected with the newly added condenser and a driven heat medium pipeline connected to the outside, and the new condenser is further added. The refrigerant liquid pipeline is connected to the first condenser by adding a second throttle valve, and the newly added absorber and the newly added condenser are respectively connected with the externally heated medium pipeline to form a single-stage double effect. Two-stage regenerative third-class absorption heat pump.

 54. The regenerative third type absorption heat pump is a new type of third throttle valve added in the regenerative third type absorption heat pump according to item 53, and the second new generator is heated. The medium pipeline is connected to the outside to adjust the generator to add a refrigerant vapor channel. After the second generator is connected, a second generator is added, and then the refrigerant liquid pipeline is added with a third throttle valve and a new condenser. Connected - the refrigerant vapor released by the generator is used as the driving heat medium for the addition of the second generator to form a two-stage regenerative third type absorption heat pump with a single stage double effect as the first stage.

 55. The regenerative third type absorption heat pump is a new type of third generator, new absorber, new solution pump added to the regenerative third type absorption heat pump described in items 19-24. And adding a solution heat exchanger, adding a second generator having a refrigerant vapor passage and connecting the first condenser to adjust a new second generator having a refrigerant vapor passage and connecting the new absorber, adding an absorber There is also a dilute solution pipeline connected to the newly added third generator via a new solution pump and a new solution heat exchanger, a new third generator and a concentrated solution pipeline via a new solution heat exchanger and new absorption. The third generator further has a refrigerant vapor passage communicating with the first condenser and a driving heat medium conduit communicating with the outside, and the newly added absorber and the heated medium conduit are connected to the outside to form The single-stage three-effect is the first-stage two-stage regenerative third-class absorption heat pump.

 56. The regenerative third type absorption heat pump is a new type of third throttle valve added in the regenerative third type absorption heat pump described in item 55, and the new third generator is heated. The medium pipe is connected to the outside to adjust to the generator or the new first generator is added with a refrigerant vapor channel. After the new third generator is connected, a third generator is added, and then the refrigerant liquid pipeline is added. The flow valve is connected to the first condenser--the generator or the newly added refrigerant vapor generated by the first generator is used as the driving heat medium of the newly added third generator to form a two-stage return with the single-stage three-effect as the first stage. Thermal third type absorption heat pump.

 57. The regenerative third type absorption heat pump is a new type of third generator, new absorber, new solution pump added to the regenerative third type absorption heat pump described in items 19-24. New solution heat exchanger, new condenser and new third throttle valve, new second generator added refrigerant vapor channel to connect with new absorber, new absorber and dilute solution pipeline The new solution pump and the new solution heat exchanger are connected with the newly added third generator, and the third generator and the concentrated solution pipeline are connected to the newly added absorber through the new solution heat exchanger, and the third is added. The generator also has a refrigerant vapor channel connected to the newly added condenser and a driven heat medium pipe connected to the outside, and a new condenser and a refrigerant liquid pipeline are added through the third section to the first condenser. Connected, the newly added absorber and the newly added condenser also have a medium to be heated to communicate with the outside, forming a two-stage regenerative third type absorption heat pump with a single stage and three effects as the first stage.

 58. The regenerative third type absorption heat pump is a new type of fourth throttle valve added to the regenerative third type absorption heat pump described in item 57, and the new third generator is heated. The medium pipe is connected to the outside to adjust to the generator or the new first generator is added with a refrigerant vapor channel. After the third generator is connected, the third generator is added and the refrigerant liquid pipeline is added. The flow valve is connected to the first condenser--the generator or the newly added refrigerant vapor generated by the first generator is used as the driving heat medium of the newly added third generator to form a two-stage return with the single-stage three-effect as the first stage. Thermal third type absorption heat pump.

 BRIEF DESCRIPTION OF THE DRAWINGS:

BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing the first structure and flow of a two-way circulating regenerative absorption generating system according to the present invention. 2 is a schematic view showing the second structure and flow of a two-way circulating regenerative absorption-generation system according to the present invention. 3 is a schematic view showing the first structure and flow of a single-pass circulating regenerative absorption-generation system according to the present invention. 4 is a schematic view showing the second structure and flow of a single-pass circulating regenerative absorption-generation system according to the present invention. Figure 5 is a schematic view showing the first structure and flow of a single-stage single-effect regenerative third-class absorption heat pump according to the present invention. 6 is a schematic view showing the second structure and flow of a single-stage single-effect regenerative third-class absorption heat pump according to the present invention. 7 is a schematic view showing the third structure and flow of a single-stage single-effect regenerative third-class absorption heat pump according to the present invention. FIG. 8 is a fourth structural and flow diagram of a single-stage single-effect regenerative third-class absorption heat pump according to the present invention. 9 is a schematic view showing the fifth structure and flow of a single-stage single-effect regenerative third-class absorption heat pump according to the present invention. Figure 10 is a schematic view showing the sixth structure and flow of a single-stage single-effect regenerative third-class absorption heat pump according to the present invention.

 Fig. 11 is a schematic view showing the seventh structure and flow of a single-stage single-effect regenerative third-stage absorption heat pump according to the present invention.

 Figure 12 is a schematic view showing the structure and flow of a single-stage parallel double-effect regenerative third-class absorption heat pump according to the present invention.

 Figure 13 is a schematic view showing the first structure and flow of a single-stage series double-effect regenerative third-stage absorption heat pump according to the present invention.

 Figure 14 is a schematic view showing the second structure and flow of a single-stage series double-effect regenerative third-stage absorption heat pump according to the present invention.

 Figure 15 is a schematic view showing the structure and flow of a single-stage parallel three-effect regenerative third-class absorption heat pump according to the present invention.

 Figure 16 is a schematic view showing the first structure and flow of a single-stage series three-effect regenerative third type absorption heat pump according to the present invention.

 Figure 17 is a schematic view showing the second structure and flow of a single-stage series three-effect regenerative third-class absorption heat pump according to the present invention.

 Figure 18 is a schematic view showing the first structure and flow of a single-generator two-stage regenerative third-stage absorption heat pump according to the present invention.

 Figure 19 is a schematic view showing the second structure and flow of a single-generator two-stage regenerative third-stage absorption heat pump according to the present invention.

 Figure 20 is a schematic view showing the third structure and flow of a single-generator two-stage regenerative third-stage absorption heat pump according to the present invention.

 Figure 21 is a schematic view showing the fourth structure and flow of a single-generator two-stage regenerative third-stage absorption heat pump according to the present invention.

 Figure 22 is a schematic view showing the fifth structure and flow of a single-generator two-stage regenerative third-stage absorption heat pump according to the present invention.

 Figure 23 is a schematic view showing the sixth structure and flow of a single-generator two-stage regenerative third-stage absorption heat pump according to the present invention.

 Figure 24 is a schematic view showing the first structure and flow of a two-stage two-stage regenerative third type absorption heat pump according to the present invention.

 Figure 25 is a schematic view showing the second structure and flow of a two-stage two-stage regenerative third type absorption heat pump according to the present invention.

 Figure 26 is a schematic view showing the third structure and flow of a two-stage two-stage regenerative third type absorption heat pump according to the present invention.

 Figure 27 is a schematic view showing the fourth structure and flow of a two-stage two-stage regenerative third type absorption heat pump according to the present invention.

 Figure 28 is a schematic view showing the fifth structure and flow of a two-stage two-stage regenerative third type absorption heat pump according to the present invention.

 Figure 29 is a schematic view showing the sixth structure and flow of a two-stage two-stage regenerative third type absorption heat pump according to the present invention.

30 is a seventh structure and flow of a two-stage two-stage regenerative third type absorption heat pump provided in accordance with the present invention. Explain the book diagram.

 Figure 31 is a schematic view showing the structure and flow of a single-stage double-effect regenerative third-class absorption heat pump with an additional condenser as an additional high-temperature heating end according to the present invention.

 Figure 32 is a schematic view showing the structure and flow of an adjustable single-stage double-effect regenerative third-stage absorption heat pump with an additional condenser as an additional high-temperature heating end according to the present invention.

 Figure 33 is a schematic view showing the first structure and flow of a two-stage regenerative third type absorption heat pump with a single stage double effect as the first stage according to the present invention.

 Figure 34 is a schematic view showing the second structure and flow of a two-stage regenerative third type absorption heat pump with a single stage double effect as the first stage according to the present invention.

In the figure, 1 - absorption-evaporator, 2 - absorber, 3 - first absorption - generator, 4 - second absorption - generator, 5 - generator (rectification column) / first generator, 6 - First solution pump, 7-second solution pump, 8-third solution pump, 9-solution heat exchanger/first solution heat exchanger, 10" second solution heat exchanger, 11 first steam compartment, 12—Second steam separation chamber, 13—fourth solution pump, 14-solution throttle valve/first solution throttle valve, 15-second solution throttle valve, 16—first condenser, 17—second condensation , ₁₈ - first evaporator, 19 - second evaporator, 20" throttle / first throttle, 21 - coolant pump / first coolant pump, 22 - second coolant pump , 23—third evaporator, 24—second throttle valve, 25—third throttle valve, 26—fourth throttle valve; A—new generator/new first generator, B—new Throttle valve / new first throttle valve, C new solution heat exchanger / new first solution heat exchanger, D "new solution pump / new first solution pump, E - new second Generator, F - new second throttle , G—addition of second solution heat exchanger, H—addition of second solution pump, I-new absorption-evaporator, J-added refrigerant pump, K-addition absorber, L-addition Condenser, M - new third throttle valve, N - new first flow regulating valve, 0 "- new second flow regulating valve.

 What needs to be specified is:

 (1) In Figs. 1-4, the absorption-evaporator 1, the first absorption-generator 1 and the second steam separation chamber 12 achieve regenerative heat.

 (2) The main function of the absorption-evaporator 1 is to heat the refrigerant liquid flowing therethrough into a refrigerant vapor, and the second absorption-generator 4 mainly functions to vaporize the solution flowing therethrough, and sometimes Partial low temperature heat load can be taken separately.

 (3) When a working medium typified by an aqueous ammonia solution is used, the generator is referred to as a rectification column at this time, and the first rectification column is further increased in communication with the outside by the heated medium line.

 (4) When a working medium typified by an aqueous ammonia solution is used, the first steam dividing chamber 11 involved in the aqueous ammonia solution increases the connection of the cooling medium piping to the outside if necessary.

 (5) taking the example shown in FIG. 1 , the dilute solution of the first absorption-generator 3 is depressurized and lowered by the second solution heat exchanger 10, and then flows through the second absorption-generator 4 to achieve partial vaporization; At this time, the second solution heat exchanger 10 has two functions - achieving heat exchange between the solutions and throttling and depressurizing the dilute solution, and if necessary, adding a solution section to the dilute solution line at the outlet of the first absorption-generator 3 The flow valve, or the solution throttle valve instead of the second solution heat exchanger 10 _ has little effect on the heat pump performance specifications.

 (6) "Parallel" in "single-stage parallel double-effect regenerative third-class absorption heat pump" means that the regenerative third-type absorption heat pump realizes double-effect flow when the solution circulation is parallel; "single-stage parallel three The same is true.

 (7) The "series" in the "single-stage series double-effect regenerative third-class absorption heat pump" refers to the recirculating type III absorption heat pump to realize the double-effect process when the solution circulation is in series; "single-stage series three The same is true.

 (8) The term "single stage" in terms such as "single stage double effect" refers to the name in the first type of absorption heat pump, and "double effect" also follows the occurrence of high temperature driving heat medium in the first type of absorption heat pump. The angle of action is called.

 (9) In Fig. 21, when the pressure difference between the newly added absorber K and the first absorption-generator 3 is too small, the new solution heat exchanger C may not be provided or the absorber K and the first absorption may be added - A new solution pump D is disposed on the dilute solution line connecting the generator 3.

(10) In Figs. 18-23 and 26-30, the temperature at which the second absorption-generator 4 externally supplies the heat load is lower than the temperature at which the absorber 2 provides the external heat load, at which time the second absorption-generator 4 bears Heating the solution flowing through the solution and partially vaporizing the solution; when the external heat load demand is suitable, the second absorption-generator 4 can simultaneously supply external heat; similarly, there are cases Description

The absorption-evaporator 1 in Figures 20-23.

detailed description:

 The invention will be described in detail below with reference to the accompanying drawings and examples. In the case of a specific example, the structure and process are not repeated if not necessary.

 The two-way regenerative absorption-generation system shown in Figure 1 is implemented in this way -

1 structurally, it mainly consists of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, a third solution pump, a first solution a heat exchanger, a second solution heat exchanger, a first steam dividing chamber and a second steam dividing chamber, wherein the absorption-evaporator 1 has a dilute solution line connected to the first absorption-generator 3 via the third solution pump 8 The first absorption-generator 3 and the dilute solution line are in communication with the first steam dividing chamber 1 through the second solution heat exchanger 10 and the second absorption-generator 4, and the first steam dividing chamber 11 also has a concentrated solution tube. The second solution pump 7, the second solution heat exchanger 10 and the first absorption-generator 3 are in communication with the second distribution chamber 12, and the second distribution chamber 12 has a concentrated solution line connected to the absorber 2, The absorber 2 also has a dilute solution line connected to the absorption-evaporator 1, and the second absorption-generator 4 has a dilute solution line connected to the generator 5 via the first solution pump 6 and the first solution heat exchanger 9 And the concentrated solution line is connected to the second absorption-generator 4 via the first solution heat exchanger 9 The absorption-evaporator 1 also has a refrigerant vapor passage communicating with the outside, and the external refrigerant liquid line is connected to the absorption-evaporator 1 and then the absorption-evaporator 1 and the refrigerant vapor passage are connected to the first absorption-generator 3 The absorber 2 further has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, and the second steam dividing chamber 12 and the refrigerant vapor passage are in communication with the absorption-evaporator 1, the first steam dividing chamber 1 1 also has a refrigerant vapor passage communicating with the outside, and the second absorption-generator 4 further has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, and the generator 5 further has a refrigerant vapor passage It communicates with the outside and has a drive heat medium line that communicates with the outside.

 2 In the process, the refrigerant vapor from the outside enters the absorber 2, is absorbed by the concentrated solution from the second steam dividing chamber 12 and radiates heat to the heated medium, and the diluted solution of the absorber 2 enters the absorption-evaporator 1, and the absorption comes from The refrigerant vapor of the second steam dividing chamber 12 radiates heat to the refrigerant liquid flowing through the absorption-evaporator 1, and the refrigerant liquid from the outside flows through the absorption-evaporator 1, absorbs heat into the refrigerant vapor, and goes to the first The absorption-generator 3 is provided; the dilute solution of the absorption-evaporator 1 is pressurized by the third solution pump 8 into the first absorption-generator 3, absorbing the refrigerant vapor from the absorption-evaporator 1 and radiating heat to the flow through a solution of the absorption-generator 3, the dilute solution of the first absorption-generator 3 is cooled and depressurized by the second solution heat exchanger 10, then flows through the second absorption-generator 4, and the endothermic portion is vaporized and then enters the first The steam dividing chamber 11 releases the solution entering the first steam dividing chamber 11 and supplies the refrigerant vapor to the outside. The concentrated solution of the first steam dividing chamber 11 passes through the second solution pump 7 and the second solution heat exchanger 10 and then flows through the first portion. An absorption-generator 3, the endothermic portion is vaporized and then enters the second steam dividing chamber 12, The solution entering the second steam dividing chamber 12 releases and supplies refrigerant vapor to the absorption-evaporator 1, the concentrated solution of the second steam dividing chamber 12 enters the absorber 2; the refrigerant vapor from the outside enters the second absorption-generator 4 Absorbed by the concentrated solution from the generator 5 and respectively exothermic to the heated medium and the solution flowing through the second absorption-generator 4, the dilute solution of the second absorption-evaporator 4 is passed through the first solution pump 6 and the first The solution heat exchanger 9 enters the generator 5, and the solution that drives the heat medium to heat the generator 5 releases the refrigerant vapor to the outside, and the concentrated solution of the generator 5 releases heat through the first solution heat exchanger 9 and is depressurized to enter the second absorption. - Generator 4, forming a two-way regenerative absorption-generation system.

 The two-way circulating regenerative absorption-generation system shown in Fig. 2, compared with that shown in Fig. 1, the changes shown in Fig. 2 are: 1 The absorption-evaporator 1 increases the heat medium line to communicate with the outside; The solution throttle valve 14 is increased, the absorber 2 has a dilute solution line connected to the absorption-evaporator 1 via the solution throttle 14; 3 the fourth solution pump 13 is added, and the second steam separation chamber 12 is passed through the fourth solution pump 13 The absorber 2 is connected; 4 the first steam dividing chamber 11 increases the cooling medium line to communicate with the outside; 5 externally supplies refrigerant vapor to the absorption-evaporator 1, and the absorption-evaporator 1 also radiates heat to the heated medium.

 The single-cycle regenerative absorption-generation system shown in Figure 3 is implemented as follows:

1 structurally, it mainly consists of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, a third solution pump, a first solution a heat exchanger, a second solution heat exchanger, a first steam dividing chamber and a second steam dividing chamber, wherein the absorption-evaporator 1 has a dilute solution line connected to the first absorption-generator 3 via the third solution pump 8 The first absorption-generator 3 and the dilute solution line are in communication with the second absorption-generator 4 via the second solution heat exchanger 10, and the second absorption-generator 4 has a dilute solution line through the first solution pump 6 and The first solution heat exchanger 9 is in communication with the generator 5, The generator 5 also has a concentrated solution line connected to the first steam dividing chamber 11 via the first solution heat exchanger 9 and the second absorption-generator 4, and the first steam dividing chamber 11 has a concentrated solution line through the second solution. The pump 7, the second solution heat exchanger 10 and the first absorption-generator 3 are in communication with the second steam dividing chamber 12, and the second steam dividing chamber 12 has a concentrated solution line communicating with the absorber 2, and the absorber 2 is further The dilute solution line is connected to the absorption-evaporator 1, the absorption-evaporator 1 and the refrigerant vapor channel are connected to the outside, and the external refrigerant liquid line is connected to the absorption-evaporator 1 and the absorption-evaporator 1 is cooled again. The agent vapor passage is in communication with the first absorption-generator 3, and the absorber 2 further has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, and the second steam dividing chamber 12 also has a refrigerant vapor passage and The absorption-evaporator 1 is connected, the first steam dividing chamber 11 and the refrigerant vapor passage are connected to the outside, and the second absorption-generator 4 further has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside. The generator 5 also has a refrigerant vapor passage to communicate with the outside and a drive heat medium conduit External communication.

 2 In the process, the refrigerant vapor from the outside enters the absorber 2, is absorbed by the concentrated solution from the second steam dividing chamber 12 and radiates heat to the heated medium, and the diluted solution of the absorber 2 enters the absorption-evaporator 1, and the absorption comes from The refrigerant vapor of the second steam dividing chamber 12 radiates heat to the refrigerant liquid flowing through the absorption-evaporator 1, and the refrigerant liquid from the outside flows through the absorption-evaporator 1, absorbs heat into the refrigerant vapor, and goes to the first The absorption-generator 3 is provided; the dilute solution of the absorption-evaporator 1 is pressurized by the third solution pump 8 into the first absorption-generator 3, absorbing the refrigerant vapor from the absorption-evaporator 1 and radiating heat to the flow through a solution of the absorption-generator 3, the dilute solution of the first absorption-generator 3 is cooled and depressurized by the second solution heat exchanger 10, then enters the second absorption-generator 4, absorbs the refrigerant vapor from the outside and separates it Heated by the heated medium and the solution flowing through the second absorption-generator 4, the dilute solution of the second absorption-evaporator 4 enters the generator 5 via the first solution pump 6 and the first solution heat exchanger 9, driving the heat medium Heating the solution entering the generator 5 to release the refrigerant vapor The concentrated solution of the generator 5 is exothermic and depressurized by the first solution heat exchanger 9 and then flows through the second absorption-generator 4, and the endothermic portion is vaporized and then enters the first steam dividing chamber 11 to enter the first steam dividing portion. The solution of the chamber 11 is released and externally supplied with refrigerant vapor. The concentrated solution of the first steam dividing chamber 11 passes through the second solution pump 7 and the second solution heat exchanger 10 and then flows through the first absorption-generator 3 and the heat absorption portion. After vaporization, the second steam dividing chamber 12 is introduced, the solution entering the second steam dividing chamber 12 is released and the refrigerant vapor is supplied to the absorption-evaporator 1, and the concentrated solution of the second steam dividing chamber 12 enters the absorber 2 to form a single loop. Regenerative absorption-generation system.

 The single-cycle regenerative absorption-generation system shown in Fig. 4, compared with that shown in Fig. 3, the changes shown in Fig. 4 are: 1 The absorption-evaporator 1 increases the heat medium line to communicate with the outside; The first solution throttle valve 14 is added, the absorber 2 has a dilute solution line connected to the absorption-evaporator 1 via the first solution throttle valve 14; 3 the fourth solution pump 13 is added, and the second steam separation chamber 12 is passed through the fourth The solution pump 13 is in communication with the absorber 2; 4 cancels the second solution heat exchanger 10, adds a second solution throttle valve 15, the first steam dividing chamber 11 has a concentrated solution line through the second solution pump 7 and the first absorption - The generator 3 is in communication with the second steam dividing chamber 12, and the first absorption-generator 3 has a dilute solution line connected to the second absorption-generator 4 via the second solution throttle valve 15; 5 externally supplying refrigerant vapor to the absorption - The evaporator 1 and the absorption-evaporator 1 are also exothermic to the heated medium.

 The single-stage single-effect regenerative third-class absorption heat pump shown in Figure 5 is implemented as follows:

1 structurally, in the regenerative absorption-generation system shown in FIG. 1, the heated medium line in which the second absorption-generator 4 communicates with the outside is canceled, and the first condenser, the second condenser, and the first The evaporator, the second evaporator, the throttle valve, the first refrigerant liquid pump and the second refrigerant liquid pump, and the refrigerant 5 passage of the generator 5 is connected to the outside to determine that the generator 5 has a refrigerant vapor passage and the first A condenser 16 is connected, the first condenser 16 and the refrigerant liquid pipeline communicate with the second evaporator 19 via the throttle valve 20, and the second absorption-generator 4 has a refrigerant vapor passage connected to the outside to determine the first The second evaporator 19 has a refrigerant vapor passage communicating with the second absorption-generator 4, and the first steam distribution chamber 11 has a refrigerant vapor passage communicating with the outside to determine that the first steam distribution chamber 11 has a refrigerant vapor passage and a second The condenser 17 is connected, and the second condenser 17 and the refrigerant liquid pipeline are connected to the first evaporator 18 via the first refrigerant liquid pump 21, and the refrigerant vapor passage of the absorption-vaporizer 1 is connected to the outside to be determined as the first An evaporator 18 has a refrigerant vapor passage communicating with the absorption-evaporator 1, and the absorber 2 has a refrigerant The steam passage is connected to the outside to determine that the first evaporator 18 has a refrigerant vapor passage communicating with the absorber 2, and the external refrigerant liquid line is connected to the absorption-evaporator 1 and then absorbed. The evaporator 1 has a refrigerant vapor passage. The communication with the first absorption-generator 3 is determined to be that the first evaporator 18 has a refrigerant liquid line connected to the absorption-evaporator 1 via the second refrigerant liquid pump 22, and the absorption-evaporator 1 has a refrigerant vapor passage and The first absorption-generator 3 is in communication, the first condenser 16 is further connected to the outside by the heated medium line, and the second condenser 17 has a cooling medium. The quality pipeline is in communication with the outside, and the first evaporator 18 and the second evaporator 19 are further connected to the outside by a residual heat medium conduit.

2 In the process, the refrigerant vapor generated by the generator 5 enters the first condenser 16, and is heated to the heated medium to form a refrigerant liquid, and the refrigerant liquid of the first condenser 16 is throttled and depressurized by the throttle valve 20 Entering the second evaporator 19, absorbing residual heat into the refrigerant vapor and providing it to the second absorption-generator 4; the refrigerant vapor generated by the first steam dividing chamber 11 enters the second condenser 17, and is cooled after being radiated to the cooling medium The refrigerant liquid of the second condenser 17 is pressurized by the first refrigerant liquid pump 21 and then enters the first evaporator 18, and the refrigerant liquid entering the first evaporator 18 is divided into two paths - the first path absorbs waste heat The refrigerant vapor is supplied to the absorber 2, and the second passage is pressurized by the second refrigerant liquid pump 22, flows through the absorption-evaporator 1, absorbs heat into the refrigerant vapor, and is supplied to the first absorption-generator 3, Form a single-stage single-effect regenerative third-class absorption heat pump.

 The single-stage single-effect regenerative third-class absorption heat pump shown in Figure 6 is realized in this way -

1 Structurally, in the regenerative absorption-generation system shown in FIG. 2, the heated medium line in which the second absorption-generator 4 is externally connected is eliminated, and the first condenser, the second condenser, and the first evaporator are added. a second evaporator, a third evaporator, a first throttle valve, a second throttle valve, a first refrigerant liquid pump, and a second refrigerant liquid pump, and the generator 5 has a refrigerant vapor passage connected to the outside It is determined that the generator 5 has a refrigerant vapor passage communicating with the first condenser 16, and the first condenser 16 and the refrigerant liquid conduit are in communication with the second evaporator 19 via the first throttle valve 20, and the second absorption is The generator 4 has a refrigerant vapor passage communicating with the outside to determine that the second evaporator 19 has a refrigerant vapor passage communicating with the second absorption-generator 4, and the first steam dividing chamber 11 has a refrigerant vapor passage communicating with the outside as The first steam dividing chamber 11 has a refrigerant vapor book passage communicating with the second condenser 17, and the second condenser 17 and the refrigerant liquid pipeline are connected to the first evaporator 18 via the first refrigerant liquid pump 21, first The evaporator 18 also has a refrigerant liquid line through the second throttle valve 24 and the third evaporator 23 Connected, the absorption-evaporator 1 has a refrigerant vapor passage communicating with the outside to determine that the third evaporator 23 has a refrigerant vapor passage communicating with the absorption-evaporator 1, and the absorber 2 having the refrigerant vapor passage communicating with the outside is determined as The first evaporator 18 has a refrigerant vapor passage communicating with the absorber 2, and the external refrigerant liquid line is connected to the absorption-evaporator 1 and then absorbed. The evaporator 1 has a refrigerant vapor passage and a first absorption-generator. 3 communication is determined as the third evaporator 23 has a refrigerant liquid pipeline connected to the absorption-evaporator 1 via the second refrigerant liquid pump 22, and then the absorption-evaporator 1 has a refrigerant vapor passage and a first absorption-generator 3 In communication, the first condenser 16 is further connected to the outside by the heating medium line, and the second condenser 17 and the cooling medium line are in communication with the outside, the first evaporator 18, the second evaporator 19 and the third evaporator 23 There are also residual heat medium pipes connected to the outside.

 2 In the process, the refrigerant vapor generated by the generator 5 enters the first condenser 16, and is heated to the heated medium to form a refrigerant liquid, and the refrigerant liquid of the first condenser 16 is throttled by the first throttle valve 20 After being pressed, the second evaporator 19 is introduced, and the residual heat is absorbed into the refrigerant vapor and supplied to the second absorption generator 4; the refrigerant vapor generated by the first steam division chamber 11 enters the second condenser 17, and is heated to the cooling medium. The refrigerant liquid, the refrigerant liquid of the second condenser 17 is pressurized by the first refrigerant liquid pump 21, and then enters the first evaporator 18, and the refrigerant liquid entering the first evaporator 18 is divided into two paths - the first road The residual heat is absorbed into the refrigerant vapor and supplied to the absorber 2, the second passage is throttled into the third evaporator 24 via the second throttle valve 24, and the refrigerant liquid entering the third evaporator 24 is divided into two paths - the first road The residual heat is absorbed into the refrigerant vapor and supplied to the absorption-evaporator 1, and the second passage is pressurized by the second refrigerant liquid pump 22, flows through the absorption-evaporator 1, absorbs heat into the refrigerant vapor, and proceeds to the first absorption-generation The device 3 provides a single-stage single-effect regenerative third-class absorption heat pump.

 The single-stage single-effect regenerative third-class absorption heat pump shown in Figure 7 is realized in this way -

1 structurally, in the regenerative absorption-generation system shown in FIG. 3, adding a first condenser, a second condenser, a first evaporator, a second evaporator, a first refrigerant liquid pump, and a second cold The liquid medium pump, the first throttle valve and the second throttle valve connect the refrigerant vapor passage of the generator 5 to the outside to determine that the generator 5 has a refrigerant vapor passage communicating with the first condenser 16, the first condenser 16 is further connected to the first evaporator 18 via the first throttle valve 20, and the refrigerant passage of the first steam distribution chamber 11 is connected to the outside to determine that the first steam distribution chamber 11 has refrigerant vapor. The passage is in communication with the second condenser 17, and the second condenser 17 and the refrigerant liquid line are in communication with the first evaporator 18 via the first refrigerant liquid pump 21, and the first evaporator 18 and the refrigerant liquid line are The second throttle valve 24 is in communication with the second evaporator 19, and the second absorption-generator 4 has a refrigerant vapor passage communicating with the outside to determine that the second evaporator 19 has a refrigerant vapor passage and a second absorption-generator 4 Connected, the absorption-evaporator 1 has a refrigerant vapor passage communicating with the outside to determine that the first evaporator 18 has a refrigerant vapor passage and Yield - communicating evaporator 1, the absorber 2 The specification has a refrigerant vapor passage communicating with the outside to determine that the first evaporator 18 has a refrigerant vapor passage communicating with the absorber 2, and the external refrigerant liquid line is connected to the absorption-evaporator 1 and then the absorption-evaporator 1 has The refrigerant vapor passage is connected to the first absorption-generator 3 to determine that the first evaporator 18 has a refrigerant liquid line that is connected to the absorption-evaporator 1 via the second refrigerant liquid pump 22, and the absorption-evaporator 1 is cooled again. The agent vapor channel is in communication with the first absorption-generator 3, the first condenser 16 is further connected to the outside by the heated medium line, and the second condenser 17 and the cooling medium line are in communication with the outside, the first evaporator 18 and The second evaporator 19 also has a residual heat medium line connected to the outside.

 2 In the process, the refrigerant vapor generated by the generator 5 enters the first condenser 16, and is heated to the heated medium to form a refrigerant liquid, and the refrigerant liquid of the first condenser 16 is throttled by the first throttle valve 20 After being pressed, the first evaporator 18 is introduced; the refrigerant vapor generated by the first steam dividing chamber 11 enters the second condenser 17, and the refrigerant liquid is discharged into the cooling medium, and the refrigerant liquid of the second condenser 17 passes through the refrigerant. After the liquid pump 21 is boosted, it enters the first evaporator 18; the refrigerant liquid entering the first evaporator 18 is divided into three paths - the first passage absorbs the residual heat into the refrigerant vapor and supplies it to the absorber 2, and the second passage passes through the second The throttle valve 24 is throttled into the second evaporator 19, absorbing residual heat into the refrigerant vapor and supplied to the second absorption-generator 4, and the third passage is pressurized by the second refrigerant liquid pump 22 and then passed through the absorption-evaporation. 1. The heat is absorbed into the refrigerant vapor and supplied to the first absorption-generator 3 to form a single-stage single-effect regenerative third-type absorption heat pump.

 The single-stage single-effect regenerative third-class absorption heat pump shown in Figure 8 is implemented as follows:

 1 Structurally, in the recuperative absorption-generation system shown in FIG. 3, the heated medium line in which the second absorption-generator 4 communicates with the outside is canceled, and the absorption-evaporator 1 increases the heated medium line and the outside. Connecting, adding a first condenser, a second condenser, a first evaporator, a second evaporator, a first throttle valve, a first refrigerant liquid pump, and a second refrigerant liquid pump, and the generator 5 has a refrigerant The steam passage is connected to the outside to determine that the generator 5 has a refrigerant vapor passage communicating with the first condenser 16, and the first condenser 16 and the refrigerant liquid conduit are in communication with the first evaporator 18 via the first throttle valve 20, The first steam dividing chamber 11 has a refrigerant vapor passage communicating with the outside to determine that the first steam dividing chamber 11 has a refrigerant vapor passage communicating with the second condenser 17, and the second condenser 17 has a refrigerant liquid pipeline. A refrigerant liquid pump 21 is in communication with the second evaporator 19, and the second absorption-generator 4 has a refrigerant vapor passage communicating with the outside to determine that the second evaporator 19 has a refrigerant vapor passage and a second absorption-generator 4 Connected, the absorption-evaporator 1 has a refrigerant vapor channel connected to the outside It is determined that the first evaporator 18 has a refrigerant vapor passage communicating with the absorption-evaporator 1, and the absorber 2 having the refrigerant vapor passage communicating with the outside is determined such that the first evaporator 18 has a refrigerant vapor passage communicating with the absorber 2, The external refrigerant liquid line is connected to the absorption-evaporator 1 and the absorption-evaporator 1 and the refrigerant vapor channel are connected to the first absorption-generator 3 to determine that the first evaporator 18 has a refrigerant liquid line. The second refrigerant liquid pump 22 is in communication with the absorption-evaporator 1 and the absorption-evaporator 1 has a refrigerant vapor passage communicating with the first absorption-generator 3, and the first condenser 16 has a heated medium line and an external portion. In connection, the second condenser 17 further has a cooling medium line communicating with the outside, and the first evaporator 18 and the second evaporator 19 respectively have a heat remaining medium line communicating with the outside.

 2 In the process, the refrigerant vapor generated by the generator 5 enters the first condenser 16 and is heated to the heated medium to form a refrigerant liquid, and the refrigerant liquid is throttled and depressurized by the first throttle valve 20 to enter the first The evaporator 18, the refrigerant liquid entering the first evaporator 18 is divided into three paths - the first path absorbs the residual heat into the refrigerant vapor and is supplied to the absorption-evaporator 1, and the second path absorbs the residual heat into the refrigerant vapor and flows to the absorber 2, the third passage is pressurized by the second refrigerant liquid pump 22 and then flows through the absorption-evaporator 1, and absorbs heat into the refrigerant vapor and is supplied to the first absorption-generator 3; the first steam separation chamber 11 is generated. The refrigerant vapor enters the second condenser 17, and is cooled by the cooling medium to form a refrigerant liquid. The refrigerant liquid of the second condenser 17 is pressurized by the refrigerant liquid pump 21, and then enters the second evaporator 19 to absorb the residual heat. The refrigerant vapor is supplied to the second absorption-generator 4 to form a single-stage single-effect regenerative third-stage absorption heat pump.

 The single-stage single-effect regenerative third-class absorption heat pump shown in Figure 9 is implemented as follows:

1 structurally, in the regenerative absorption-generation system shown in FIG. 4, adding a first condenser, a second condenser, a first evaporator, a second evaporator, a third evaporator, a first throttle valve , the refrigerant liquid pump, the second throttle valve, the third throttle valve and the fourth throttle valve, the generator 5 has a refrigerant vapor passage and the external communication is determined as the generator 5 has a refrigerant vapor passage and the first condensation The first condenser 16 and the refrigerant liquid pipeline are connected to the second evaporator 19 via the first throttle valve 20, and the second evaporator 19 has a refrigerant liquid pipeline via the third throttle valve 25. In communication with the first evaporator 18, the first evaporator 18 and the refrigerant liquid line communicate with the third evaporator 23 via the second throttle valve 24, and the first steam dividing chamber 11 has a refrigerant vapor passage communicating with the outside. It is determined that the first steam dividing chamber 11 has a refrigerant vapor passage communicating with the second condenser 17, and the second condenser 17 and the refrigerant liquid pipeline are connected to the second evaporator 19 via the first refrigerant liquid pump 21, The second absorption-generator 4 has a refrigerant vapor passage communicating with the outside to determine that the second evaporator 19 has a refrigerant vapor passage communicating with the second absorption-generator 4, and the absorption-evaporator 1 has a refrigerant vapor passage and The external communication is determined to be that the third evaporator 23 has a refrigerant vapor passage communicating with the absorption-evaporator 1, and the absorber 2 having the refrigerant vapor passage communicating with the outside is determined as the first evaporator 18 having the refrigerant vapor passage and the absorber 2 Connected, the external refrigerant liquid line is connected to the absorption-evaporator 1 and then absorbed. The evaporator 1 and the refrigerant vapor channel are connected to the first absorption-generator 3 to determine that the first condenser 16 has a refrigerant liquid tube. After passing through the fourth throttle valve 26 and communicating with the absorption-evaporator 1, the absorption-evaporator 1 has a refrigerant vapor passage communicating with the first absorption-generator 3, and the first condenser 16 has a heated medium line and Externally connected, the second condenser 17 also has a cooling medium line communicating with the outside, the first evaporation 18, the second evaporator 19 and the evaporator 23 is also a third heat medium line respectively communicating with the outside.

 2 In the process, the refrigerant vapor generated by the generator 5 enters the first condenser 16, and is heated to the heated medium to form a refrigerant liquid, and the refrigerant liquid is divided into two paths - the first passage is said to be a flow valve through the first section. 20 throttling and then entering the second evaporator 19, the second path is throttled by the fourth throttle valve 26 and then flows through the absorption-evaporator 1, the heat is absorbed into the refrigerant vapor and is directed to the first absorption-generator 3 Providing; the refrigerant vapor generated by the first steam dividing chamber 11 enters the second condenser 17, and releases the heat to the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the second condenser 17 is pressurized by the refrigerant liquid pump 21 to enter The second evaporator 19; the refrigerant liquid entering the second evaporator 19 is divided into two paths - the first passage absorbs the residual heat into the refrigerant vapor and provides the second absorption-descriptor 4, and the second passage passes through the third throttle The valve 25 enters the first evaporator 18; the refrigerant liquid entering the first evaporator 18 is split into two paths - the first passage absorbs the residual heat into the refrigerant vapor and provides it to the absorber 2, and the second passage passes through the second throttle valve 24 After throttling, the third evaporator 23 is introduced, and the residual heat is absorbed into the refrigerant vapor and supplied to the absorption-evaporator 1 to form a single-stage single The third heat recovery absorption heat pump.

 The single-stage single-effect regenerative third-class absorption heat pump shown in Figure 10 is realized in this way -

1Structurally, in the regenerative third type absorption heat pump shown in FIG. 9, the second evaporator 19 and the third throttle valve 25 are eliminated, and the second evaporator 19 is cancelled by the third throttle valve 25 and the first The refrigerant liquid pipeline connected to the evaporator 18 connects the refrigerant liquid pipeline of the first condenser 16 to the second evaporator 19 via the first throttle line 20 to adjust the first condenser 16 to have a refrigerant liquid pipeline. The first throttle valve 20 is connected to the first evaporator 18, and the second condenser 17 has a refrigerant liquid pipeline connected to the second evaporator 19 through the refrigerant liquid pump 21 to be adjusted to have a refrigerant in the second condenser 17 The liquid line communicates with the first evaporator 18 via a refrigerant liquid pump 21, and the first evaporator 18 increases the refrigerant vapor passage to communicate with the second absorption-generator 4.

 2 In the process, the refrigerant vapor generated by the generator 5 enters the first condenser 16, and is heated to the heated medium to form a refrigerant liquid, and the refrigerant liquid is divided into two paths - the first passage is widened by the first section 20 After the throttle is depressurized, it enters the first evaporator 18, and the second passage is throttled by the fourth throttle valve 26, then flows through the absorption-evaporator 1, absorbs heat into the refrigerant vapor, and supplies the first absorption-generator 3 The refrigerant vapor generated by the first steam dividing chamber 11 enters the second condenser 17, and is cooled by the cooling medium to form a refrigerant liquid, and the refrigerant liquid of the second condenser 17 is pressurized by the refrigerant liquid pump 21 to enter the first An evaporator 18; the refrigerant liquid entering the first evaporator 18 is divided into three paths - the first path absorbs the residual heat into the refrigerant vapor and is supplied to the second absorption-generator 4, and the second path absorbs the residual heat into the refrigerant vapor and Provided to the absorber 2, the third passage enters the third evaporator 23 via the second throttle valve 24, absorbs waste heat into refrigerant vapor, and supplies it to the absorption-evaporator 1 to form a single-stage single-effect regenerative third-class absorption. Heat pump.

 Figure 10 is a schematic view showing the structure of the heat pump shown in Figure 9 without the second evaporator 19; when utilizing the latent heat of the heat recovery medium, the task of supplying the refrigerant vapor to the second absorption-generator 4 by the second evaporator 19 is The first evaporator 18 is operated by the first evaporator 18 to increase the refrigerant vapor passage to communicate with the second absorption-generator 4.

 The single-stage single-effect regenerative third-class absorption heat pump shown in Figure 11 is implemented as follows:

1 structurally, in the regenerative absorption-generation system shown in FIG. 4, the heated medium line in which the second absorption-generator 4 communicates with the outside is canceled, and the first condenser, the second condenser, and the first The evaporator, the second evaporator, the third evaporator, the first throttle valve, the first refrigerant liquid pump, the second throttle valve and the second refrigerant liquid pump, the generator 5 has a refrigerant vapor passage and an external The connection is determined to be that the generator 5 has a refrigerant vapor passage communicating with the first condenser 16, and the first condenser 16 and the refrigerant liquid line are in communication with the first evaporator 18 via the first throttle valve 20, the first evaporator 18 is further connected to the third evaporator 23 via the second throttle valve 24, and the first steam distribution chamber 1 has a refrigerant vapor passage communicating with the outside to determine that the first steam distribution chamber 11 has The refrigerant vapor passage is in communication with the second condenser 17, and the second condenser 17 and the refrigerant liquid pipeline are connected to the second evaporator 19 via the first refrigerant liquid pump 21, and the second absorption-generator 4 is cooled. The agent vapor passage is connected to the outside to determine that the second evaporator 19 has a refrigerant vapor passage communicating with the second absorption-generator 4, and the absorption-vaporizer 1 has a refrigerant vapor passage communicating with the outside to determine that the third evaporator 23 has The refrigerant vapor passage communicates with the absorption-evaporator 1, and the refrigerant 2 has a refrigerant vapor passage communicating with the outside to determine that the first evaporator 18 has a refrigerant vapor passage communicating with the absorber 2, and the external refrigerant liquid conduit After the absorption-evaporator 1 is connected, the absorption-evaporator 1 is further connected to the first absorption-generator 3, and the first evaporator 18 has a refrigerant liquid line through the second refrigerant liquid pump 22 and After the absorption-evaporator 1 is connected, the absorption-evaporator 1 has a refrigerant vapor passage communicating with the first absorption-generator 3, and the first condenser 16 is further connected to the outside by the heating medium line, and the second condenser 17 is further There is a cooling medium line communicating with the outside, a first evaporator 18, a second evaporator 19 and Three evaporator 23 also respectively communicate with the external heat medium line.

 2 In the process, the refrigerant vapor generated by the generator 5 enters the first condenser 16 and is heated to the heated medium to form a refrigerant liquid. The refrigerant liquid is throttled by the first throttle valve 20 and then enters the first evaporation. The refrigerant liquid entering the first evaporator 18 is divided into three paths - the first passage absorbs the residual heat into the refrigerant vapor and supplies it to the absorber 2, and the second passage passes through the second section and flows 24 throttling and then enters the third The evaporator 23 absorbs the residual heat into the refrigerant vapor and supplies it to the absorption-evaporator 1. The third passage is pressurized by the second refrigerant liquid pump 22, and then the absorption-evaporator 1 absorbs heat into the refrigerant vapor and is directed to the first absorption. - generator 3 provides; refrigerant steam generated by the first steam dividing chamber 11

 Book

The steam enters the second condenser 17, and releases the heat to the cooling medium to form a refrigerant liquid. The refrigerant liquid of the second condenser 17 is pressurized by the first refrigerant liquid pump 21, enters the second evaporator 19, and absorbs the residual heat to be cooled. The agent vapor is supplied to the second absorption-generator 4 to form a single-stage single-effect regenerative third-stage absorption heat pump.

 The single-stage parallel double-effect regenerative third-class absorption heat pump shown in Figure 12 is realized in this way -

1Structurally, in the regenerative third type absorption heat pump shown in FIG. 5, a new generator, a new throttle valve and a new solution heat exchanger are added, and the first solution pump 6 is provided with a dilute solution pipeline. The new solution heat exchanger C is connected with the newly added generator A, and the newly added generator A and the concentrated solution pipeline are connected to the second absorption-generator 4 via the new solution heat exchanger C, and the generator 5 is cooled. The agent steam passage is connected to the first condenser 16 to adjust to the generator 5 having the refrigerant vapor passage connected with the newly added generator A, adding the generator A and then the refrigerant liquid pipeline via the newly added throttle valve B and the first The condenser 16 is connected - the refrigerant vapor released by the generator acts as a driving heat medium for the newly added generator, and the new generator A and the refrigerant vapor passage are in communication with the first condenser 16.

 2 In the process, a portion of the dilute solution of the second absorption-generator 4 enters the new generator A via the first solution pump 6 and the new solution heat exchanger C, and the refrigerant vapor from the generator 5 flows through the new generator. A. Heating the solution entering the newly added generator A to release the refrigerant vapor, adding the refrigerant vapor generated by the generator A to the first condenser 16; adding the concentrated solution of the generator A through the newly added solution heat exchanger C Entering the second absorption-generator 4, the refrigerant vapor flowing through the newly added generator A is released into a refrigerant liquid, and then throttled into the first condenser 16 through the addition of a new throttle valve B to form a single-stage parallel double effect. A regenerative third type absorption heat pump.

 The single-stage series double-effect regenerative third-class absorption heat pump shown in Figure 13 is realized as follows:

 1Structally, in the regenerative third type absorption heat pump shown in 7, the addition of a new generator, a new throttle valve and a new solution heat exchanger are added, and the generator 5 has a concentrated solution pipeline through the first The solution heat exchanger 9 and the second absorption-generator 4 are connected to the first steam distribution chamber 11 to be adjusted so that the generator 5 has a concentrated solution pipeline connected to the newly added generator A via the new solution heat exchanger C, and newly added occurs. The A solution and the concentrated solution line are connected to the first steam dividing chamber 11 via the first solution heat exchanger 9 and the second absorption-generator 4, and the second absorption-generator 4 has a dilute solution line through the first solution. The pump 6 and the first solution heat exchanger 9 are connected to the generator 5 to be adjusted to a second absorption-generator 4 having a dilute solution line through the first solution pump 6, the first solution heat exchanger 9 and the new solution heat exchanger C is connected with the generator 5, and the generator 5 has a refrigerant vapor passage connected to the first condenser 16 to be adjusted to be a generator 5 having a refrigerant vapor passage connected with the newly added generator A, and then adding a generator A and then a refrigerant. The liquid line is connected to the first condenser 16 via a new throttle valve B - the refrigerant vapor released by the generator Additional heat generator as driving medium, the new generator A further passage communicating with the first refrigerant vapor condenser 16.

2 In the process, the dilute solution of the second absorption-generator 4 enters the generator 5 through the first solution pump 6, the first solution heat exchanger 9, and the newly added solution heat exchanger C, and the refrigerant vapor generated by the generator 5 The new generator A is provided as its driving heat medium, and the concentrated solution of the generator 5 enters the new generator A through the new solution heat exchanger C; the cold flowing through the new generator A The specification agent steam is heated into the dilute solution of the newly added generator A to release and supplies the refrigerant vapor to the first condenser 16, and the concentrated solution of the new generator A is added to the first solution heat exchanger 9 and the second absorption-generator 4 Entering the first steam dividing chamber 11 , the refrigerant vapor flowing through the newly added generator A is exothermic to form a refrigerant liquid, and then throttled into the first condenser 16 by adding a new throttle valve B to form a single-stage series double-effect back. Thermal third type absorption heat pump.

 The single-stage series double-effect regenerative third-class absorption heat pump shown in Figure 12 is realized as follows:

 1Structurally, in the regenerative third type absorption heat pump shown in Fig. 5, adding a new generator, a new throttle valve, a new solution heat exchanger and a new solution pump, the second absorption-occurrence occurs. The dilute solution line has a dilute solution line connected to the generator 5 via the first solution pump 6 and the first solution heat exchanger 9 to be adjusted to a second absorption-generator 4 having a dilute solution line through the first solution pump 6 and the first solution The heat exchanger 9 is connected to the newly added generator A, and the new generator A and the concentrated solution pipeline are connected to the generator 5 via the new solution pump D and the new solution heat exchanger C, and the generator 5 has a concentrated solution. The pipeline is connected to the second absorption-generator 4 via the first solution heat exchanger 9 to be adjusted to have a concentrated solution of the generator 5 through the new solution heat exchanger C and the first solution heat exchanger 9 and the second absorption - The generator 4 is connected, and the generator 5 has a refrigerant vapor passage communicating with the first condenser 16 to adjust the generator 5 to have a refrigerant vapor passage connected with the newly added generator A, and then adding the generator A and then the refrigerant liquid pipe. The road is connected to the first condenser 16 by adding a new throttle B. The refrigerant released by the generator is steamed. As the new generator driven heat medium, the new generator A further passage communicating with the first refrigerant vapor condenser 16.

 2 In the process, the refrigerant vapor released by the generator 5 is supplied to the newly added generator A as its driving heat medium, and the diluted solution of the second absorption-generator 4 passes through the first solution pump 6 and the first solution heat exchanger 9 Entering the new generator A, the refrigerant vapor flowing through the newly added generator A heats the solution into the refrigerant vapor, and the refrigerant vapor generated by the generator A is added to the first condenser 16, and a new generator is added. The concentrated solution of A enters the generator 5 via the new solution pump D and the new solution heat exchanger C; the concentrated solution of the generator 5 enters the second absorption through the new solution heat exchanger C and the first solution heat exchanger 9 - The generator 4, the refrigerant vapor flowing through the newly added generator A is exothermic to form a refrigerant liquid, and then throttled into the first condenser 16 through the addition of a new throttle valve B to form a single-stage series double-effect regenerative type third. Absorption heat pump.

 The single-stage parallel three-effect regenerative third-class absorption heat pump shown in Figure 15 is realized in this way -

1Structurally, in the regenerative third type absorption heat pump shown in FIG. 5, the addition of the first generator, the addition of the second generator, the addition of the first throttle valve, and the addition of the second throttle valve are added. Adding a first solution heat exchanger and adding a second solution heat exchanger, the first solution pump 6 adding a dilute solution pipeline is respectively connected with the newly added first generator A by adding a first solution heat exchanger C and The second solution heat exchanger G is newly connected with the newly added second generator E, and the first generator A and the concentrated solution pipeline are newly added by adding the first solution heat exchanger C and the second absorption-generator. 4 connected, a new second generator E and a concentrated solution pipeline are connected to the second absorption-generator 4 via the newly added second solution heat exchanger G, and the generator 5 has a refrigerant vapor passage and a first condenser The 16-connected adjustment is such that the generator 5 has a refrigerant vapor passage connected with the newly added first generator A, and the first generator A is added, and then the refrigerant liquid pipeline is added with the first throttle valve B and the first condenser. 16 connected - the refrigerant vapor generated by the generator is used as the driving heat medium for adding the first generator, adding the first hair The refrigerant A and the new second generator E are connected to each other to add a second generator E, and then the refrigerant liquid line is connected to the first condenser 16 via a new second throttle valve F- The refrigerant vapor generated by the first generator is added as a driving heat medium for adding the second generator, and the second generator F and the refrigerant vapor passage are connected to communicate with the first condenser 16.

2 In the process, a part of the dilute solution of the second absorption-generator 4 enters the newly added first generator A through the first solution pump 6 and the newly added first solution heat exchanger C, and the release of the generator 5 is added to the first The generator A supplies the refrigerant vapor as its driving heat medium, and the refrigerant vapor flows through the newly added first generator A, the solution heated into the liquid is released, and the refrigerant vapor is supplied to the newly added second generator E. The concentrated solution of the first generator A is introduced into the second absorption-generator 4 by adding the first solution heat exchanger C; the other portion of the dilute solution of the second absorption-generator 4 is passed through the first solution pump 6 and adding a second The solution heat exchanger G enters a new second generator E, and the refrigerant vapor from the newly added first generator A flows through the newly added second generator E, and the solution heated therein is released and directed to the first condenser 16 Providing refrigerant vapor, adding a concentrated solution of the second generator E to the second absorption-generator 4 by adding a second solution heat exchanger G; forming a refrigerant vapor flowing through the newly added first generator A to form a heat release The refrigerant liquid is throttled into the first condenser 16 by adding a first throttle valve B, and flows through the newly added second generator E. Cold refrigerant vapor formation heat The agent liquid is throttled into the first condenser 16 by adding a second throttle valve F to form a single-stage parallel three-effect regenerative third type absorption heat pump.

 The single-stage series three-effect regenerative third-class absorption heat pump shown in Figure 16 is realized in this way -

1Structurally, in the third type of absorption heat pump shown in FIG. 7, the heated medium line in which the second absorption-generator 4 communicates with the outside is cancelled, the first generator is added, the second generator is added, A first throttle valve is added, a second section is added, a first solution heat exchanger is added, and a second solution heat exchanger is added. The generator 5 has a concentrated solution line through the first solution heat exchanger. 9 and the second absorption-generator 4 is connected to the first steam distribution chamber 1 1 to be adjusted to have a concentrated solution line of the generator 5 connected to the newly added first generator A via the first solution heat exchanger 9 , adding a first The generator A also has a concentrated solution pipeline, a first solution heat exchanger C is added to communicate with the newly added second generator E, a second generator E and a concentrated solution pipeline are added, and a second solution heat exchanger is added. G and the second absorption-generator 4 are in communication with the first steam dividing chamber 11, and the second absorption-generator 4 has a dilute solution line connected to the generator 5 via the first solution pump 6 and the first solution heat exchanger 9 Adjusted to the second absorption-generator 4 with a dilute solution line through the first solution pump 6, adding a second solution heat exchanger 0 It is said that the newly added first solution heat exchanger C and the first solution heat exchanger 9 are in communication with the generator 5, and the generator 5 has a refrigerant vapor passage communicating with the first condenser 16 to adjust the generator 5 to have a refrigerant vapor passage. After the new first generator A is connected, the first generator A is newly added, and the refrigerant liquid pipeline is connected with the first condenser 16 via the newly added first throttle valve B - the refrigerant vapor generated by the generator is used as Adding the first generator's driving heat medium, adding the first generator A and the refrigerant vapor channel to connect with the new second generator E. The book adds a second generator E and then a refrigerant liquid pipeline. A second throttle valve F is added to communicate with the first condenser 16 - a refrigerant coolant generated by the first generator is added as a driving heat medium for adding a second generator, and a second generator F is added. The agent vapor passage is in communication with the first condenser 16.

 2 In the process, the dilute solution of the second absorption-generator 4 enters through the first solution pump 6, the addition of the second solution heat exchanger 0, the addition of the first solution heat exchanger C and the first solution heat exchanger 9 The refrigerant vapor generated by the generator 5 is supplied to the newly added first generator A as its driving heat medium, and the concentrated solution of the generator 5 enters the newly added first generator A through the first solution heat exchanger 9 The refrigerant vapor flows through the newly added first generator A, the solution heated into the solution is released, and the cold refrigerant vapor is supplied to the newly added second generator E, and the concentrated solution of the first generator A is newly added by adding the first solution. The heat exchanger C enters the newly added second generator E, and the refrigerant vapor from the newly added first generator A flows through the newly added second generator E, and the solution heated into it is released and supplied to the first condenser 16 The refrigerant vapor, the new concentrated solution of the second generator E is added to the first steam dividing chamber 1 1 by adding the second solution heat exchanger G and the second absorption-generator 4; flowing through the newly added first generator A The refrigerant liquid formed by the refrigerant vapor exotherm is throttled by the addition of the first throttle valve B. a condenser 16, the refrigerant liquid formed by the heat release of the refrigerant vapor of the newly added second generator E is throttled into the first condenser 16 by the addition of the second throttle valve F, forming a single-stage series triple effect Thermal third type absorption heat pump.

 The single-stage series three-effect regenerative third-class absorption heat pump shown in Figure 17 is realized as follows:

1Structurally, in the regenerative third type absorption heat pump shown in FIG. 8, the heated medium line in which the absorption-evaporator 1 is connected to the outside is eliminated, and the first generator is added, and the second generator is added. , adding a first throttle valve, adding a second throttle valve, adding a first solution heat exchanger, adding a second solution heat exchanger, adding a first solution pump, and adding a second solution pump, The second absorption-generator 4 has a dilute solution line connected to the generator 5 via the first solution pump 6 and the first solution heat exchanger 9 to be adjusted to a second absorption-generator 4 having a dilute solution line through the first solution pump 6 and the first solution heat exchanger 9 is connected with the newly added second generator E, and the second generator E and the concentrated solution pipeline are newly added by adding the second solution pump H and adding the second solution heat exchanger G. Connected with the newly added first generator A, the first generator A and the concentrated solution pipeline are connected to the generator 5 via the newly added first solution pump D and the newly added first solution heat exchanger C, and the generator 5 The concentrated solution pipeline is connected to the first steam splitting chamber 1 through the first solution heat exchanger 9 and the second absorption-generator 4 to adjust the generator 5 to be rich The liquid line is connected to the first steam dividing chamber 1 1 via the newly added first solution heat exchanger C, the newly added second solution heat exchanger G, the first solution heat exchanger 9 and the second absorption generator 4 The generator 5 has a refrigerant vapor passage communicating with the first condenser 16 to adjust the generator 5 to have a refrigerant vapor passage connected with the newly added first generator A, adding a first generator A and then a refrigerant liquid pipeline. A first throttle valve B is added to communicate with the first condenser 16 - the refrigerant vapor generated by the generator is used as a driving heat medium for adding the first generator, and the first generator A and the refrigerant vapor channel are added. After adding the second generator E, the second generator E is added, and then the refrigerant liquid pipeline is added by the second throttle valve F. Instruction manual

Communicating with the first condenser 16 - adding the refrigerant vapor generated by the first generator as the driving heat medium for adding the second generator, adding the second generator F and the refrigerant vapor passage and the first condenser 16 connected.

 2 In the process, the dilute solution of the second absorption-generator 4 enters the newly added second generator E through the first solution pump 6 and the first solution heat exchanger 9, and the concentrated solution of the second generator E is newly added. The second solution pump H and the newly added second solution heat exchanger G enter the newly added first generator A, and the new concentrated solution of the first generator A is newly added with the first solution pump D and the newly added first solution is exchanged. The device C enters the generator 5, and the concentrated solution of the generator 5 is introduced through the addition of the first solution heat exchanger C, the addition of the second solution heat exchanger G, the first solution heat exchanger 9 and the second absorption-generator 4 The first steam dividing chamber 11; the refrigerant vapor generated by the generator 5 is supplied to the newly added first generator A as a driving heat medium thereof, and the solution flowing through the refrigerant vapor of the newly added first generator A is heated therein. Release and add refrigerant vapor to the newly added second generator E as its driving heat medium, and the solution flowing through the refrigerant vapor added by the second generator E is heated to release and provide cold to the first condenser 16. Vapor; a refrigerant formed by the exotherm of the refrigerant vapor added to the first generator A The liquid is throttled into the first condenser 16 by adding a first throttle valve B, and the refrigerant liquid formed by the heat release of the refrigerant vapor added by the second generator E is throttled by the addition of the second throttle valve F. The first condenser 16 is entered to form a single-stage series three-effect regenerative third type absorption heat pump.

 The single-generator two-stage regenerative third-class absorption heat pump shown in Figure 18 is implemented as follows:

 1Structurally, in the regenerative third type absorption heat pump shown in Fig. 5, the new solution heat exchanger, the new absorption-evaporator and the newly added refrigerant liquid pump are added, and the absorption-evaporator 1 is diluted. The solution line is connected to the first absorption-generator 3 via the third solution pump 8 to be adjusted to absorb - the evaporator 1 has a dilute solution line connected to the newly added absorption-evaporator I via the new solution heat exchanger C, The absorption-evaporator I and the dilute solution line are connected to the first absorption-generator 3 via the third solution pump 8 and the new solution heat exchanger C, and the first evaporator 18 has a refrigerant vapor channel and absorption respectively. The evaporator 1 and the absorber 2 are connected to be adjusted so that the first evaporator 8 has a refrigerant vapor passage communicating with the newly added absorption-evaporator I, and the first evaporator 18 is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump J and After the new absorption-evaporator I is connected, the absorption-evaporator I is added and the refrigerant vapor channel is connected to the absorption-evaporator 1 and the absorber 2, respectively.

 2 In the process, the dilute solution of the absorption-evaporator 1 is introduced into the new absorption-evaporator I through the new solution heat exchanger C, absorbing the refrigerant vapor from the first evaporator 18, and releasing the heat and flowing through the newly absorbed absorption- The refrigerant liquid of the evaporator I, the dilute solution of the new absorption-evaporator I is introduced into the first absorption-generator 3 via the third solution pump 8 and the new solution heat exchanger C; the refrigerant of the first evaporator 18 The liquid is pressurized by the newly added refrigerant liquid pump J, and then flows through the new absorption-evaporator I, the heat-absorbing refrigerant vapor is supplied to the absorber 2, and the refrigerant is supplied to the absorber by the new absorption-evaporator. Steam single generator two-stage regenerative third type absorption heat pump.

 The single-generator two-stage regenerative third-stage absorption heat pump shown in Figure 19 is implemented as follows:

 1Structure, in the regenerative third type absorption heat pump shown in Figure 5, adding a new solution heat exchanger, a new solution pump, a new absorption-evaporator and a new refrigerant liquid pump, the absorber 2 The dilute solution pipeline is connected with the absorption-evaporator 1 to adjust to the absorber 2, the dilute solution pipeline is connected to the newly added absorption-evaporator I via the new solution heat exchanger C, and the new absorption-evaporator I is added. The dilute solution pipeline is connected to the absorption-evaporator 1 via the new solution pump D and the new solution heat exchanger C, and the refrigerant vapor passage of the first evaporator 18 is connected to the absorption-evaporator 1 and the absorber 2, respectively. The first evaporator 8 has a refrigerant vapor passage communicating with the newly added absorption-evaporator I, and the first evaporator 18 adds a refrigerant liquid pipeline through the newly added refrigerant liquid pump J to communicate with the newly added absorption-evaporator I. A new absorption-evaporator I and a refrigerant vapor channel are connected to the absorption-evaporator 1 and the absorber 2, respectively.

 2 In the process, the dilute solution of the absorber 2 enters the new absorption-evaporator I through the new solution heat exchanger C, absorbs the refrigerant vapor from the first evaporator 18, and releases the heat through the new absorption-evaporator. The refrigerant liquid of I, the dilute solution of the new absorption-evaporator I is added to the absorption-evaporator 1 via the new solution pump D and the new solution heat exchanger C; the coolant of the first evaporator 18 is newly added. After the refrigerant liquid pump J is pressurized, it flows through the newly added absorption-evaporator I, absorbs the heat into the refrigerant vapor, and supplies it to the absorber 2, forming a single occurrence of the refrigerant vapor supplied to the absorber by the newly added absorption-evaporator. Two-stage regenerative third-class absorption heat pump.

 The single-generator two-stage regenerative third-stage absorption heat pump shown in Figure 20 is implemented as follows:

1Structurally, in the regenerative third type absorption heat pump shown in FIG. 7, the second absorption-generator 4 is disconnected from the outside. In the heated medium pipeline of the instruction manual, a new throttle valve, a new solution heat exchanger, a new absorption-evaporator and a new solution pump are added, and the second steam separation chamber 12 has a concentrated solution pipeline and an absorber 2 The communication is adjusted to be that the second steam distribution chamber 12 has a concentrated solution pipeline connected to the absorber 2 via the new solution pump D and the new solution heat exchanger C, and the absorber 2 has a dilute solution pipeline connected to the absorption-evaporator 1 Adjusted to the absorber 2, the dilute solution line is connected to the new absorption-evaporator I via the new solution heat exchanger C, and the new absorption-evaporator I and the dilute solution line are connected to the absorption-evaporator 1 The first evaporator 18 has a refrigerant vapor passage connected to the absorber 2 to be adjusted so that the first evaporator 18 has a refrigerant vapor passage communicating with the newly added absorption-evaporator I, and the first condenser 16 adds a refrigerant liquid pipeline through the new The additional section B is connected to the new absorption-evaporator I, and the new absorption-evaporator I is connected to the absorber 2 via a refrigerant vapor channel.

 2 In the process, the refrigerant vapor of the first evaporator 18 is supplied to the newly added absorption-evaporator I, and one coolant liquid of the first condenser 16 is throttled by the new throttle valve B and then flows through the newly absorbed absorption- The evaporator I absorbs heat into the refrigerant vapor and supplies it to the absorber 2; the concentrated solution of the second steam separation chamber 12 enters the absorber 2 through the newly added solution pump D and the new solution heat exchanger C, and absorbs from the newly absorbed - the refrigerant vapor of the evaporator I is exothermic to the heated medium, the dilute solution of the absorber 2 is introduced into the new absorption-evaporator I via the new solution heat exchanger C, and the refrigerant vapor from the first evaporator 18 is absorbed. And exothermic to the refrigerant liquid flowing through the new absorption-evaporator I, adding a dilute solution of the absorption-evaporator I into the absorption-evaporator 1, forming a refrigerant vapor supplied to the absorber by the new absorption-evaporator The single-generator two-stage regenerative third-class absorption heat pump.

 The single-generator two-stage regenerative third-stage absorption heat pump shown in Figure 21 is implemented as follows:

 1Structurally, in the regenerative third type absorption heat pump shown in FIG. 8, the heated medium line that the absorption-evaporator 1 communicates with the outside is canceled, and the new throttle valve and the new solution heat exchanger are added. And adding a absorber, the absorption-evaporator 1 has a dilute solution line connected to the first absorption-generator 3 via the third solution pump 8 to be adjusted to absorb - the evaporator 1 has a dilute solution line through the third solution pump 8 And the new solution heat exchanger C is connected with the newly added absorber K, and the new absorber K and the dilute solution line are connected to the first absorption-generator 3 via the new solution heat exchanger C, and the absorber 2 has The medium to be heated is connected to the outside to be adjusted so that the first condenser 16 is provided with a refrigerant liquid pipeline. After the new throttle tube B is connected with the absorber 2, the absorber 2 is added, and the refrigerant vapor channel and the newly added absorber are added. K connected, the new absorber K and the heated medium line communicate with the outside.

 2 In the process, the refrigerant liquid of the first condenser 16 flows through the absorber 2 through the newly added throttling B-throttle, absorbs the heat into the refrigerant vapor, and supplies it to the newly added absorber K, and the absorption-evaporator 1 The dilute solution enters the new absorber through the third solution pump 8 and the new solution heat exchanger C, absorbs the refrigerant vapor from the absorber 2 and radiates heat to the heated medium, and adds a dilute solution of the absorber K through the new The solubilizing solution heat exchanger C enters the first absorption-generator 3 to form a single-stage two-stage regenerative third type absorption heat pump that supplies refrigerant vapor to the newly added absorber from the absorber.

 The single-generator two-stage regenerative third-class absorption heat pump shown in Fig. 22 is realized in this way -

1Structurally, in the regenerative third-type absorption heat pump shown in FIG. 5, an additional refrigerant liquid pump, a new solution heat exchanger and a new absorber are added, and the generator 5 has a concentrated solution pipeline. The first solution heat exchanger 9 is connected to the second absorption-generator 4 to be adjusted to have a concentrated solution line of the generator 5 connected to the newly added absorber K via the first solution heat exchanger 9, and the new absorber K is also diluted. The solution line is connected to the second absorption-generator 4 via the new solution heat exchanger C, and the second absorption-generator 4 has a dilute solution line through the first solution pump 6 and the first solution heat exchanger 9 The device 5 is connected to the second absorption-generator 4, and the dilute solution line is connected to the generator 5 via the first solution pump 6, the new solution heat exchanger C and the first solution heat exchanger 9, and the absorber 2 has The medium to be heated is connected to the outside to be adjusted to add a refrigerant liquid line to the second evaporator 19. The new refrigerant liquid pump J is connected to the absorber 2, and the absorber 2 has a refrigerant vapor channel and a new absorber K. Connected, the new absorber K and the heated medium line are connected to the outside.

2 In the process, the refrigerant liquid of the second evaporator 19 is pressurized by the newly added refrigerant liquid pump J, and then flows through the absorber 2, absorbs heat into the refrigerant vapor and supplies it to the newly added absorber K, and the second absorption - the dilute solution of the generator 4 enters the generator 5 via the first solution pump 6, the new solution heat exchanger C and the first solution heat exchanger 9, and the concentrated solution of the generator 5 enters the new solution through the first solution heat exchanger 9 The absorption absorber ^: absorbs the refrigerant vapor from the absorber 2 and radiates heat to the heated medium, and the diluted solution of the newly added absorber K enters the second absorption-generator 4 through the newly added solution heat exchanger C, and is formed by The single-generator two-stage regenerative third-stage absorption heat pump in which the absorber supplies refrigerant vapor to the newly added absorber. The single-generator two-stage regenerative third-stage absorption heat pump shown in Figure 23 is realized as follows:

 1Structurally, in the regenerative third type absorption heat pump shown in FIG. 5, an additional refrigerant liquid pump, a new solution heat exchanger, a new absorber and a new solution pump are added, and the generator 5 has The concentrated solution pipeline is connected to the second absorption-generator 4 via the first solution heat exchanger 9 to be adjusted to the generator 5 having the concentrated solution pipeline passing through the first solution heat exchanger 9 and the newly added solution heat exchanger C and the second The absorption-generator 4 is connected, and the second absorption-generator 4 has a dilute solution line connected to the generator 5 through the first solution pump 6 and the first solution heat exchanger 9 to be adjusted to a second absorption-generator 4 The solution line is connected to the newly added absorber K via the first solution pump 6 and the new solution heat exchanger C, and the addition of the absorber K and the dilute solution line via the new solution pump D and the first solution heat exchanger 9 It is connected with the generator 5, and the absorber 2 has a medium to be heated and communicated with the outside to adjust the second evaporator 19 to add a refrigerant liquid pipeline. After the new refrigerant liquid pump J is connected with the absorber 2, the absorber 2 is further There is a refrigerant vapor channel connected to the newly added absorber K, and the new absorber K is also heated. Conduit communicating with the outside.

 2 In the process, the refrigerant liquid of the second evaporator 19 is pressurized by the newly added refrigerant liquid pump J, and then flows through the absorber 2, absorbs heat into the refrigerant vapor and supplies it to the newly added absorber K, and the second suction says The dilute solution of the receiver-generator 4 enters the new absorber via the first solution pump 6 and the new solution heat exchanger C! ^ Absorbs the refrigerant vapor from the absorber 2 and exotherms the heated medium, and the dilute solution of the newly added absorber enters the generator 5 through the new solution pump D and the first solution heat exchanger 9, the concentrated solution of the generator 5 Passing through the first solution heat exchanger 9 and the newly added solution heat exchanger C into the second absorption-generator 4, forming an absorber from the absorber to the new absorber

 Book

A single-generator two-stage regenerative third-stage absorption heat pump that provides refrigerant vapor.

 The dual-generator two-stage regenerative third-stage absorption heat pump shown in Figure 24 is implemented as follows:

 1Structurally, in the regenerative third type absorption heat pump shown in FIG. 5, a new generator, a new solution heat exchanger, a new solution pump and a new absorber are added, and the generator 5 has a refrigerant. The steam passage is connected to the first condenser 16 to be adjusted so that the generator 5 has a refrigerant vapor passage communicating with the newly added absorber K, and the new absorber K and the dilute solution pipeline are heated by the new solution pump D and the newly added solution. The device C is connected with the newly added generator A, and the newly added generator A and the concentrated solution pipeline are connected to the newly added absorber K through the new solution heat exchanger C, and the newly added generator A also has a refrigerant vapor channel and The first condenser 16 communicates with the drive heat medium line to communicate with the outside, and the new absorber K and the heated medium line communicate with the outside.

 2 In the process, the refrigerant vapor released by the generator 5 enters the newly added absorber K, is absorbed by the concentrated solution from the new generator 并 and radiates heat to the heated medium, and the diluted solution of the absorber K is newly added through the new solution. The pump D and the new solution heat exchanger C enter the newly added generator A, drive the solution of the heat medium to enter the newly added generator A to release and supply the refrigerant vapor to the first condenser 16, and add the concentrated solution of the generator A. The newly added solution heat exchanger C enters the new absorber K to form a double generator two-stage regenerative third type absorption heat pump which supplies the refrigerant vapor to the newly added absorber.

 The dual-generator two-stage regenerative third-class absorption heat pump shown in Figure 25 is realized in this way -

1Structurally, in the regenerative third type absorption heat pump shown in FIG. 8, the heated medium line that the absorption-evaporator 1 communicates with the outside is canceled, and the new generator, the new solution heat exchanger, and the new one are added. Adding solution pump, adding absorber, adding condenser and adding new throttle, generator 5 adding refrigerant vapor channel to connect with new absorber K, adding absorber K and dilute solution pipeline added The solution pump D and the new solution heat exchanger C are connected with the newly added generator A, and the newly added generator A and the concentrated solution line are connected to the newly added absorber K via the newly added solution heat exchanger C, and a new generator is added. A also has a refrigerant vapor passage communicating with the newly added condenser L. The new condenser L and the refrigerant liquid pipeline are connected to the first condenser 16 via the newly added throttle valve B, and the new generator A and the drive are added. The heat medium pipe is connected to the outside, and the newly added absorber K and the newly added condenser L are also respectively connected to the outside by the heated medium pipe.

2 In the process, a part of the refrigerant vapor of the generator 5 enters the newly added absorber K, is absorbed by the concentrated solution from the newly added generator 并 and radiates heat to the heated medium, and the diluted solution of the absorber K is newly added through the new solution. Pump D and new solution heat exchanger C enter new generator A, drive the heat medium to heat the solution of the new generator A and release the refrigerant vapor to the new condenser L, and enter the cold of the new condenser L. The agent steam exotherms in the heated medium to form a refrigerant liquid, and the new condenser L refrigerant liquid is throttled by the new throttle valve B and then enters the first condenser 16 to add a concentrated solution of the generator A through the newly added solution. The heat exchanger C enters the new absorber K to form a two-stage two-stage regenerative third type absorption heat pump in which the generator supplies refrigerant vapor to the first condenser and the newly added absorber, respectively. The dual generator two-stage regenerative third-stage absorption heat pump shown in Figure 26 is realized as follows:

 1Structurally, in the regenerative third type absorption heat pump shown in FIG. 5, a new generator, a new solution heat exchanger, a new solution pump and a new absorber are added, and the first evaporator 18 is provided. The refrigerant vapor passages are respectively connected with the absorption-evaporator 1 and the absorber 2 to be adjusted so that the first evaporator 18 has a refrigerant vapor passage communicating with the newly added absorber K, and the newly added absorber K and the dilute solution pipeline are newly added. The solution pump D and the new solution heat exchanger C are connected with the newly added generator A, and the newly added generator A and the concentrated solution line are connected to the newly added absorber K via the newly added solution heat exchanger C, and a new generator is added. A also has a refrigerant vapor passage that communicates with the absorption-evaporator 1 and the absorber 2, respectively. The new generator A also has a driving heat medium line that communicates with the outside, and the new absorber K has a heated medium line and an external unit. Connected.

 2 In the process, the refrigerant vapor of the first evaporator 18 enters the newly added absorber K, is absorbed by the concentrated solution from the new generator 并, and radiates heat to the heated medium, and the diluted solution of the newly added absorber K is newly added. The solution pump D and the new solution heat exchanger C enter the newly added generator A, drive the solution of the heat medium to enter the new generator A to release and supply the refrigerant vapor to the absorber 2, and add the concentrated solution of the generator A. The new solution says that heat exchanger C enters the new absorber K, forming a two-stage two-stage regenerative third-type absorption heat pump that supplies refrigerant vapor to the absorber from the new generator.

 The dual generator two-stage regenerative third type absorption heat pump shown in Fig. 27 is realized in this way - in the regenerative third type absorption heat pump shown in Fig. 26, the new condenser and the new section are added. The flow valve, the newly added generator A additional refrigerant vapor passage is connected with the newly added condenser L, and the newly added cold coagulator L and the refrigerant liquid pipeline are connected to the first evaporator 18 via the newly added throttle valve B, The new condenser L and the heated medium line communicate with the outside to form a double generator two-stage regenerative third type absorption heat pump which supplies refrigerant vapor to the newly added condenser and absorber respectively by the newly added generator. .

 The dual generator two-stage regenerative third-stage absorption heat pump shown in Figure 28 is implemented as follows:

 1Structurally, in the regenerative third type absorption heat pump shown in FIG. 5, an additional refrigerant liquid pump, a new generator, a new solution heat exchanger, a new solution pump and a new absorber are added. The generator 5 has a refrigerant vapor passage communicating with the first condenser 16 to adjust the generator 5 to have a refrigerant vapor passage communicating with the newly added absorber K, adding a new absorber K and a dilute solution pipeline via a new solution pump. D and the new solution heat exchanger C are connected with the newly added generator A, and the newly added generator A and the concentrated solution line are connected to the newly added absorber K via the new solution heat exchanger C, and the absorber 2 has been The heating medium pipeline is connected to the outside to adjust the second evaporator 19 to add a refrigerant liquid pipeline. After the new refrigerant liquid pump J is connected with the absorber 2, the absorber 2 has a refrigerant vapor passage connected with the newly added absorber K. The newly added generator A also has a refrigerant vapor passage communicating with the first condenser 16 and a driving heat medium pipeline communicating with the outside, and the newly added absorber K and the heated medium pipeline are connected to the outside.

 2 In the process, the refrigerant liquid of the second evaporator 19 is pressurized by the newly added refrigerant liquid pump J, flows through the absorber 2, absorbs heat into the refrigerant vapor and is supplied to the newly added absorber K, and the generator 5 is released. The refrigerant vapor is supplied to the newly added absorber K; the refrigerant vapor entering the newly added absorber K is absorbed by the concentrated solution from the newly added generator A and radiated to the heated medium, and the diluted solution of the new absorber K is newly added. The so-solution pump D and the new solution heat exchanger C enter the new generator A, drive the solution of the heat medium to enter the new generator A to release and supply the refrigerant vapor to the first condenser 16, and add the generator A. The concentrated solution enters the new absorber K through the newly added solution heat exchanger C, forming a double-stage two-stage regenerative third-type absorption heat pump in which the absorber and the generator jointly supply the refrigerant vapor to the newly added absorber.

 The dual-generator two-stage regenerative third-stage absorption heat pump shown in Figure 29 is implemented as follows:

 1Structally, in the regenerative third-class absorption heat pump shown in Figure 5, add new refrigerant liquid pump, new generator, new solution heat exchanger, new solution pump and new absorption-evaporation The first evaporator 18 has a refrigerant vapor channel connected to the absorption-evaporator 1 and the absorber 2, respectively, and the first evaporator 18 has a refrigerant vapor channel connected to the newly added absorption-evaporator I, and newly absorbed. - The evaporator I and the dilute solution pipeline are connected to the new generator via the new solution pump D and the new solution heat exchanger C, and the new generator A and the concentrated solution pipeline are added to the new solution heat exchanger. C is connected with the new absorption-evaporator I, and the first evaporator 18 is provided with a refrigerant liquid pipeline. The new refrigerant liquid pump J is connected with the new absorption-evaporator I, and the new absorption-evaporator I is cooled. The agent vapor passages are in communication with the absorber 2 and the absorption-evaporator 1, respectively, and the new generator A and the refrigerant vapor passage are in communication with the absorption-evaporator 1 and the absorber 2, respectively.

2 In the process, the refrigerant vapor generated by the first evaporator 18 enters the new absorption-evaporator I, and is added from the new generator A. The concentrated solution of the specification absorbs and exotherms the refrigerant liquid flowing through the new absorption-evaporator I, and the dilute solution of the new absorption-evaporator I is added to the new solution pump D and the new solution heat exchanger C. Generator A, driving the heat medium to heat the solution of the newly added generator A to release and supply the refrigerant vapor to the absorber 2, and adding the concentrated solution of the generator A to the new solution heat exchanger C to enter the new absorption-evaporator I: one coolant liquid of the first evaporator 18 is pressurized by the newly added refrigerant liquid pump J, flows through the new absorption-evaporator I, absorbs heat into the refrigerant vapor, and is supplied to the absorber 2, and is formed by adding The absorption-evaporator and the new generator provide a dual-generator two-stage regenerative third-stage absorption heat pump that supplies refrigerant vapor to the absorber.

 The dual generator two-stage regenerative third-stage absorption heat pump shown in Figure 30 is implemented as follows:

 In the regenerative third type absorption heat pump shown in FIG. 28, a new condenser is added and a second throttle valve is added, and the newly added generator A has a refrigerant vapor passage connected to the first condenser 16 for adjustment. In order to add a new generator A, a refrigerant vapor passage is connected with the newly added condenser L, and a new condenser L and a refrigerant liquid pipeline are connected to the first condenser 16 by adding a second section flow F, the generator 5 and the absorber 2 respectively add a refrigerant vapor channel to communicate with the first condenser 16, the new condenser L and the heated medium pipe communicate with the outside, formed by the absorber and the generator together to the first condenser and A double-generator two-stage regenerative third-stage absorption heat pump with a new absorber for refrigerant vapor is added.

 The single-stage double-effect regenerative third-stage absorption heat pump with the new condenser as the additional high-temperature heating end shown in Figure 31 is realized in this way - the single-stage double-effect regenerative third class shown in Figure 12. In the absorption heat pump, a new condenser is added and a second throttle valve is added. The generator 5 is provided with a refrigerant vapor passage to communicate with the newly added condenser L. The new condenser L and the refrigerant liquid pipeline are newly added. The second throttle valve F is in communication with the first condenser 16, and the new condenser L and the heated medium pipeline are connected to the outside to form a single-stage double-effect regenerative type with an additional condenser as an additional high-temperature heating end. Three types of absorption heat pumps.

 The adjustable single-stage double-effect regenerative third-stage absorption heat pump with the additional condenser as the additional high-temperature heating end shown in Fig. 32 is realized in this way - the regenerative third type absorption shown in Fig. 31 In the heat pump, a first flow regulating valve is added and a second flow regulating valve is added, and the first condenser 16 is connected to the outside by the heating medium pipe to be adjusted to an external heated medium pipe and a first condenser. After the 16th communication, the first condenser 16 and the heated medium pipeline are respectively connected to the outside through the newly added first flow throttle valve N, and the newly added second flow regulating valve 0 is connected with the newly added condenser L, and will be newly added. The condenser L is connected to the outside by the heating medium pipe to be adjusted to be the first condenser. The heated medium pipe is connected to the new condenser L by the addition of the second flow throttle valve 0, and the new condenser L is added. The heated medium line communicates with the outside to form an adjustable type of regenerative third type absorption heat pump.

 The two-stage regenerative third-class absorption heat pump with single-stage double-effect first stage shown in Figure 33 is realized as follows:

1Structurally, in the single-stage double-effect regenerative third-class absorption heat pump shown in Fig. 12, a new second generator, a new absorber, a new solution pump and a new solution heat exchanger are added. The newly added first generator A has a refrigerant vapor passage connected to the first condenser 16 to be adjusted to add a new first generator A. The refrigerant vapor passage is connected with the newly added absorber K, and the new absorber K is also diluted. The solution line is connected to the newly added second generator E via the new solution pump D and the new solution heat exchanger C, and the second generator E and the concentrated solution line are added through the new solution heat exchanger C and the new The increase absorber K is connected, and the second generator E is further provided with a refrigerant vapor passage to communicate with the first condenser 16 and a drive heat medium pipeline to communicate with the outside, and the new absorber K and the heated medium pipeline are added. Connected to the outside.

 2 In the process, the second-stage process for raising the residual heat temperature is carried out as follows: A part of the refrigerant vapor generated by the generator A is added to the newly added absorber K, and is absorbed by the concentrated solution from the newly added second generator. Hot to the heated medium, the dilute solution of the new absorber 经 is added to the new second generator 经 through the new solution pump D and the new solution heat exchanger C, and the heat medium is heated to enter the new second generator Ε The solution is released and the refrigerant vapor is supplied to the first condenser 16, and the concentrated solution of the second generator 新增 is added to the newly added absorber 经 through the new solution heat exchanger C to form a single stage double effect as the first stage. Two-stage regenerative third-class absorption heat pump.

The two-stage regenerative third-class absorption heat pump with single stage double effect as the first stage shown in Fig. 34 is realized by the structure of the single-stage double-effect regenerative type shown in Fig. 12 In the absorption-type heat pump, the addition of the second generator, the new absorber, the new solution pump, the new solution heat exchanger, the new condenser, the addition of the second throttle valve and the addition of the third section Flow valve, new first generator A added refrigerant vapor channel and new absorber K connected, new absorber Κ and dilute solution pipeline via new solution pump D and new solution heat exchanger C and new The second generator is connected to the second generator, and the second generator and the concentrated solution line are connected to the newly added absorber through the new solution heat exchanger C. The second generator is added and the refrigerant vapor channel is added. Connected with the new condenser L, the generator 5 adds a refrigerant vapor channel to the newly added second generator, and then adds a second generator, and then the refrigerant liquid pipeline is added with a third throttle valve. New condenser L connection - part of the refrigerant vapor generated by the generator 5 is used as the driving heat medium for adding the second generator ,, and the new condenser L and the refrigerant liquid line are added by the second throttle valve. F is in communication with the first condenser 16, and the newly added absorber Κ and the newly added condenser L are also respectively connected to the outside by the heated medium line.

 2 In the process, the second-stage process for raising the residual heat temperature is carried out as follows: A part of the refrigerant vapor generated by the first generator is added to the newly added absorber K, and is absorbed by the concentrated solution from the newly added second generator. And exothermic to the heated medium, the dilute solution of the new absorber 经 is added to the new second generator 经 through the new solution pump D and the new solution heat exchanger C, and the refrigerant vapor from the generator 5 flows through the new Increasing the second generator Ε, heating the solution into the newly added second generator 释放 and providing the refrigerant vapor to the newly added condenser L, adding the concentrated solution of the second generator 经 through the new solution heat exchanger C After adding the absorber Κ, the refrigerant vapor flowing through the newly added second generator is released into the refrigerant liquid, and then added to the new condenser L by adding a third throttle valve; entering the new condenser The refrigerant vapor of L is exothermic to the refrigerant medium to form a refrigerant liquid, and the refrigerant liquid of the new condenser L is throttled into the first condenser 16 by adding a second throttle valve F to form a single-stage double effect. The first stage of the two-stage regenerative third type absorption heat pump.

 The effect that can be achieved by the technology of the present invention - the regenerative absorption-generation system and the regenerative third-type absorption heat pump proposed by the present invention have the following effects and advantages:

 1. The proposed regenerative absorption-generation system has a reasonable structure and adjustable heat recovery.

 2. The proposed series of regenerative third-class absorption heat pumps can utilize the lower temperature waste heat resources to improve the utilization of waste heat resources.

 3. The proposed series of regenerative third-class absorption heat pumps enrich the absorption heat pump, which can better match the heat pump heat supply and the user heat.

 4. By using the series of regenerative third-type absorption heat pumps provided by the invention, the working parameters and performance indexes of the single heat pump unit can be continuously matched, and the working parameters and performance indexes between adjacent heat pump units can be realized. Continuous connection.

 5. The proposed series of regenerative third-class absorption heat pumps can select the degree of heat recovery according to the residual heat parameters and the heating temperature, which is beneficial to the heat pump unit to maintain a high performance index and improve energy utilization efficiency.

Claims

Claim 1. A regenerative absorption-generation system, which is mainly composed of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, and a third a solution pump, a first solution heat exchanger, a second solution heat exchanger, a first steam dividing chamber and a second steam dividing chamber, the absorption-evaporator (1) has a dilute solution line through the third solution pump (8) Connected to the first absorption-generator (3), the first absorption-generator (3) and the dilute solution line through the second solution heat exchanger (10) and the second absorption-generator (4) is in communication with the first steam dividing chamber (11), the first steam dividing chamber (11) and the concentrated solution pipeline passing through the second solution pump (7), the second solution The heat exchanger (10) and the first absorption-generator (3) are in communication with the second steam dividing chamber (12), and the second steam dividing chamber (12) and the concentrated solution line are connected to the absorber (2) for absorption. The (2) also has a dilute solution line connected to the absorption-evaporator (1), and the second absorption-generator (4) has a dilute solution line through the first solution pump (6) and the first solution heat exchanger ( 9) communicating with the generator (5), the generator (5) and the concentrated solution line are connected to the second absorption-generator (4) via the first solution heat exchanger (9), and the absorption-evaporator (1) There is also a refrigerant vapor passage that communicates with the outside or a refrigerant vapor passage that communicates with the outside and a heated medium conduit that communicates with the outside, and an external refrigerant liquid line and an absorption-evaporator. (1) After the absorption-evaporator (1), the refrigerant vapor channel is connected to the first absorption-generator (3), and the absorber (2) also has a refrigerant vapor channel connected to the outside and a heated medium. The pipeline is connected to the outside, the second steam compartment (12) and the refrigerant vapor passage are connected to the absorption-evaporator (1), and the first steam compartment (11) and the refrigerant vapor passage are connected to the outside or respectively There is a refrigerant vapor passage communicating with the outside and a cooling medium conduit communicating with the outside, the second absorption-generator (4) and the refrigerant vapor passage communicating with the outside or respectively having a refrigerant vapor passage communicating with the outside and having a The heating medium pipeline is connected to the outside, and the generator (5) further has a refrigerant vapor passage communicating with the outside and a driving heat medium pipeline communicating with the outside to form a two-way circulating heat recovery absorption-generation system; Replace the second solution heat exchanger with a solution throttle (14) (10), changing the first absorption-generator (3) having a dilute solution line through the second solution heat exchanger (10) and the second absorption-generator (4) to the first distribution chamber (11) a first absorption-generator (3) having a dilute solution line connected to the first steam dividing chamber (11) via a solution throttle valve (14) and a second absorption-generator (4), the first steam dividing chamber (11) The concentrated solution line is changed to the first through the second solution pump (7), the second solution heat exchanger (10), and the first absorption-generator (3) and the second steam distribution chamber (12) The split steam chamber (11) has a concentrated solution line connected to the second steam split chamber (12) via the second solution pump (7) and the first absorption-generator (3). 2. A regenerative absorption-generation system, which is mainly composed of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, and a third a solution pump, a first solution heat exchanger, a second solution heat exchanger, a first steam dividing chamber, a second steam dividing chamber, a fourth solution pump and a solution throttle valve, and the absorption-evaporator (1) has a dilute solution The pipeline is connected to the first absorption-generator (3) via a third solution pump (8), the first absorption-generator (3) and the dilute solution pipeline are passed through the second solution heat exchanger (10) and the second The absorption-generator (4) is in communication with the first steam dividing chamber (11), the first steam dividing chamber (11) and the concentrated solution pipeline passing through the second solution pump (7) and the second solution heat exchanger (10) And the first absorption-generator (3) is in communication with the second steam dividing chamber (12), and the second steam dividing chamber (12) and the concentrated solution pipeline are connected to the absorber (2) via the fourth solution pump (13) , the absorber (2) and the dilute solution line are connected to the absorption-evaporator (1) via the solution throttle valve (14), and the second absorption-generator (4) has a dilute solution tube The first solution pump (6) and the first solution heat exchanger (9) are in communication with the generator (5), and the generator (5) and the concentrated solution line are passed through the first solution heat exchanger (9) and the second The absorption-generator (4) is connected, and the absorption-evaporator (1) also has a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, and an external refrigerant liquid line and an absorption-evaporator ( 1) After the absorption-evaporator (1), the refrigerant vapor channel is connected to the first absorption-generator (3), and the absorber (2) also has a refrigerant vapor channel connected to the outside and a heated medium tube. The road is connected to the outside, the second steam dividing chamber (12) and the refrigerant vapor passage are connected to the absorption-evaporator (1), and the first steam dividing chamber (11) and the refrigerant vapor passage are connected to the outside or respectively The refrigerant vapor passage communicates with the outside and has a cooling medium conduit communicating with the outside, and the second absorption-generator (4) and the refrigerant vapor passage are connected to the outside or respectively have a refrigerant vapor passage communicating with the outside and being heated The medium pipe is connected to the outside, and the generator (5) also has a refrigerant vapor pass The channel is connected to the outside and has a driving heat medium pipe connected to the outside to form a two-way circulating heat recovery absorption-generation system; wherein, the second solution throttle valve (15) can be used instead of the second solution heat exchanger (10) And changing the first absorption-generator (3) having a dilute solution line to the first distribution heat exchanger (10) and the second absorption-generator (4) to the first distribution chamber (11) One Claim Absorption-generator (3) The dilute solution line is connected to the first steam dividing chamber (11) via the second solution throttle valve (15) and the second absorption-generator (4), and the first steam dividing chamber ( 11) The concentrated solution line is changed to the first point by the second solution pump (7), the second solution heat exchanger (10), and the first absorption-generator (3) and the second distribution chamber (12) The vapor chamber (11) has a concentrated solution line connected to the second steam dividing chamber (12) via the second solution pump (7) and the first absorption-generator (3).  3. A regenerative absorption-generation system, which is mainly composed of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, and a third a solution pump, a first solution heat exchanger, a second solution heat exchanger, a first steam dividing chamber and a second steam dividing chamber, the absorption-evaporator (1) has a dilute solution line through the third solution pump (8) Connected to the first absorption-generator (3), the first absorption-generator (3) and the dilute solution line through the second solution heat exchanger (10) in communication with the second absorption-generator (4), the second absorption-generator (4) and the dilute solution line are generated by the first solution pump (6) and the first solution heat exchanger (9) The (5) is connected, the generator (5) and the concentrated solution line are connected to the first steam dividing chamber (11) via the first solution heat exchanger (9) and the second absorption-generator (4), first The steam dividing chamber (11) and the concentrated solution line are connected to the second steam dividing chamber (12) via the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3). The second steam dividing chamber (12) also has a concentrated solution line connected to the absorber (2), the absorber (2) and the dilute solution line are connected to the absorption-evaporator (1), and the absorption-evaporator (1) There is also a refrigerant vapor channel that communicates with the outside or a refrigerant vapor channel that communicates with the outside and a heated medium line that communicates with the outside. The external refrigerant liquid line communicates with the absorption-evaporator (1). - the evaporator (1) has a refrigerant vapor passage communicating with the first absorption-generator (3), and the absorber (2) also has a refrigerant vapor passage connected to the outside and having The heating medium pipe is connected to the outside, the second steam dividing chamber (12) and the refrigerant vapor channel are connected to the absorption-evaporator (1), and the first steam dividing chamber (11) and the refrigerant vapor channel are connected to the outside. The second absorption-generator (4) also has a refrigerant vapor passage communicating with the outside or respectively having a refrigerant vapor passage communicating with the outside and a heated medium conduit communicating with the outside, and the generator (5) also has a refrigerant respectively The steam passage communicates with the outside and the driven heat medium pipeline communicates with the outside to form a single-cycle circulating heat recovery absorption-generation system; wherein, the solution throttle valve (14) can be used instead of the second solution heat exchanger (10) , the first absorption-generator (3) has a dilute solution line connected to the second absorption-generator (4) via the second solution heat exchanger (10) to be changed to the first absorption-generator (3) The solution line is connected to the second absorption-generator (4) via the solution throttle valve (14), and the first solution compartment (11) has a concentrated solution line through the second solution pump (7), the second solution heat Exchanger (10) and first absorption-generator (3) and second distribution chamber (12) Changed through the first partial steam chamber (11) with a concentrated solution was pumped through a second conduit (7) and a first absorption - generator (3) and the second partial vapor chamber (12) communicates. 4. A regenerative absorption-generation system, which is mainly composed of an absorption-evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a first solution pump, a second solution pump, and a third a solution pump, a first solution heat exchanger, a second solution heat exchanger, a first steam dividing chamber, a second steam dividing chamber, a fourth solution pump and a solution throttle valve, and the absorption-evaporator (1) has a dilute solution The pipeline is connected to the first absorption-generator (3) via a third solution pump (8), and the first absorption-generator (3) and the dilute solution pipeline are passed through the second solution heat exchanger (10) and the second The absorption-generator (4) is connected, the second absorption-generator (4) and the dilute solution line are connected to the generator (5) via the first solution pump (6) and the first solution heat exchanger (9). The generator (5) and the concentrated solution line are connected to the first steam dividing chamber (11) via the first solution heat exchanger (9) and the second absorption-generator (4), and the first steam dividing chamber (11) Further, the concentrated solution line is connected to the second steam dividing chamber (12) via the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3), the second point The vapor chamber (12) and the concentrated solution line are connected to the absorber (2) via the fourth solution pump (13), the absorber (2) and the dilute solution line through the solution throttle valve (14) and absorption-evaporation The (1) is connected, and the absorption-evaporator (1) also has a refrigerant vapor passage communicating with the outside and a heated medium line communicating with the outside, and an external refrigerant liquid line communicating with the absorption-evaporator (1). After the absorption-evaporator (1), the refrigerant vapor passage is connected to the first absorption-generator (3), and the absorber (2) also has a refrigerant vapor passage to communicate with the outside and a heated medium conduit and the outside. Connected, the second steam dividing chamber U2) also has a refrigerant vapor passage communicating with the absorption-evaporator (1), the first steam dividing chamber (11) and the refrigerant vapor passage communicating with the outside, the second absorption-generator ( 4) There is also a refrigerant vapor channel that communicates with the outside or a refrigerant vapor channel that communicates with the outside and a heated medium pipe that communicates with the outside. The generator (5) also has a refrigerant vapor channel that communicates with the outside and has Driving the heat medium pipeline to communicate with the outside to form a single loop regenerative absorption-generation system; Its In the claims, the second solution throttle valve (15) may be used instead of the second solution heat exchanger (10), and the first absorption-generator (3) has a dilute solution line through the second solution heat exchanger. (10) communicating with the second absorption-generator (4) to change to the first absorption-generator (3) having a dilute solution line through the second solution throttle valve (15) and the second absorption-generator (4) Connected, the first steam dividing chamber (11) has a concentrated solution pipeline through the second solution pump (7), the second solution heat exchanger (10), and the first absorption-generator (3) and the second steam dividing chamber (12) The communication is changed to the first steam distribution chamber (11). The concentrated solution pipeline is connected to the second steam distribution chamber (12) via the second solution pump (7) and the first absorption-generator (3).  5. A regenerative third type absorption heat pump, wherein in the recuperative absorption-generation system of claim 1, the first condenser, the second condenser, the first evaporator, the second evaporator, The throttle valve, the first refrigerant liquid pump and the second refrigerant liquid pump, and the generator (5) having a refrigerant vapor passage communicating with the outside is determined as a generator (5) having a refrigerant vapor passage and a first condenser (16) Connected, the first condenser (16) and the refrigerant liquid line are connected to the second evaporator (19) via the throttle valve (20), and the second absorption-generator (4) has refrigerant vapor The passage communicating with the outside is determined as the second evaporator (19). The refrigerant vapor passage is connected to the second absorption-generator (4), and the refrigerant passage of the first steam distribution chamber (11) is connected to the outside to be determined as the first a steam compartment (11) has a refrigerant vapor passage communicating with the second condenser (17), and a second condenser (17) and a refrigerant liquid pipeline passing through the first refrigerant liquid pump (21) and the first evaporation The (18) is connected, and the absorption-evaporator (1) has a refrigerant vapor passage communicating with the outside to determine the first evaporator (18). The refrigerant vapor passage is connected to the absorption-evaporator (1), and the absorber is 2) The refrigerant vapor passage is connected to the outside to determine that the first evaporator (18) has a refrigerant vapor passage communicating with the absorber (2), and the external refrigerant liquid line is connected to the absorption-evaporator (1). The absorption-evaporator (1) is further connected to the first absorption-generator (3) by the refrigerant vapor passage to determine the first evaporator 18) or the second condenser (17) has a refrigerant liquid line connected to the absorption-evaporator (1) via the second refrigerant liquid pump (22), and then the absorption-evaporator (1) has a refrigerant vapor channel and The first absorption-generator (3) is in communication, the first condenser (16) and the heated medium line are in communication with the outside, and the second condenser (17) and the cooling medium line are in communication with the outside, the first evaporator (18) and the second evaporator (19) respectively have a residual heat medium pipe connected to the outside to form a single-stage single-effect regenerative third type absorption heat pump: wherein, when there is no second evaporator (19), A condenser (16) has a refrigerant liquid line connected to the second evaporator (19) via a throttle valve (20) to be changed to a first condenser (16) with a refrigerant liquid line through a throttle valve (20) In communication with the first evaporator (18), the first evaporator (18) increases the refrigerant vapor passage in communication with the second absorption-generator (4).  6. A regenerative third type absorption heat pump, wherein in the recuperative absorption-generation system of claim 2, the first condenser, the second condenser, the first evaporator, the second evaporator, a third evaporator, a first throttle valve, a second throttle valve, a first refrigerant liquid pump and a second refrigerant liquid pump, and the generator (5) having a refrigerant vapor passage connected to the outside is determined as a generator ( 5) The refrigerant vapor passage is connected to the first condenser (16), and the first condenser (16) and the refrigerant liquid pipeline are passed through the first throttle valve. (20) communicating with the second evaporator (19), connecting the second absorption-generator (4) with the refrigerant vapor passage to the outside to determine the second evaporator (19) having the refrigerant vapor passage and the second absorption - The generator (4) is connected, and the first steam dividing chamber (11) has a refrigerant vapor passage communicating with the outside to determine that the first steam dividing chamber (11) has a refrigerant vapor passage communicating with the second condenser (17), The second condenser (17) and the refrigerant liquid pipeline are connected to the first evaporator (18) via the first refrigerant liquid pump (21), and the first evaporator (18) and the refrigerant liquid pipeline are passed through the second The throttle valve (24) is in communication with the third evaporator (23), and the absorption-evaporator (1) has a refrigerant vapor passage communicating with the outside to determine the third evaporator (23) having a refrigerant vapor passage and absorption-evaporation The device (1) is connected, and the absorber (2) has a refrigerant vapor passage communicating with the outside to determine that the first evaporator (18) has a refrigerant vapor passage communicating with the absorber (2), and the external refrigerant liquid pipeline After the absorption-evaporator (1) is connected, the absorption-evaporator (1) is further connected to the first absorption-generator (3) and is determined to be the third evaporator (2). 3) or the first evaporator (18) has a refrigerant liquid line connected to the absorption-evaporator (1) via the second refrigerant liquid pump (22), and then the absorption-evaporator (1) has a refrigerant vapor channel and The first absorption-generator (3) is connected, the first condenser (16) and the heated medium line are in communication with the outside, and the second condenser (17) and the cooling medium line are in communication with the outside, the first evaporator (18), the second evaporator (19) and the third evaporator (23) respectively have a residual heat medium pipeline connected to the outside to form a single-stage single-effect regenerative third type absorption heat pump; wherein, no second In the evaporator (19), the first condenser (16) has a refrigerant liquid line connected to the second evaporator (19) through the first section of the flow (20) and is changed to the first condenser (16) with a refrigerant. The liquid pipeline passes through the first throttle valve (20) and the first evaporator (18) The claims are connected, and the first evaporator (18) increases the refrigerant vapor passage in communication with the second absorption-generator (4).  7. A regenerative third type absorption heat pump, in the regenerative absorption-generation system according to claim 3, wherein the second absorption-generator has a medium to be heated and communicated with the outside, the first condenser is added a second condenser, a first evaporator, a second evaporator, a first refrigerant liquid pump, a second refrigerant liquid pump or a third throttle valve, a first throttle valve and a second throttle valve, which will occur Device (5) The refrigerant vapor passage is connected to the outside to determine that the generator (5) has a refrigerant vapor passage communicating with the first condenser (16), and the first condenser (16) and the refrigerant liquid pipeline are first The throttle valve (20) is in communication with the first evaporator (18), and the refrigerant passage of the first steam distribution chamber (11) is connected to the outside to be determined as the first steam distribution chamber (11) having a refrigerant vapor passage and the first The second condenser (17) is connected, the second condenser (17) and the refrigerant liquid pipeline are passed through the first refrigerant liquid pump (21) and the first evaporator (18) or the second evaporator (19) is in communication, the first evaporator (18) and the refrigerant liquid line are connected to the second evaporator (19) via the second throttle valve (24), and the second absorption - generator (4) has a refrigerant vapor passage connected to the outside to determine the second evaporator (19). The refrigerant vapor passage is connected to the second absorption-generator (4), and the absorption-evaporator (1) is cold. The agent vapor passage is connected to the outside to be determined as a first evaporator (18) having a refrigerant vapor passage communicating with the absorption-evaporator (1), and the absorber (2) having a refrigerant vapor passage communicating with the outside as the first evaporator (18) The refrigerant vapor passage is connected to the absorber (2), and the external refrigerant liquid line is connected to the absorption-evaporator (1) and then absorbed-evaporator (1) and then the refrigerant vapor passage and the first The absorption-generator (3) is determined to be the first evaporator (18). The refrigerant liquid line is connected to the absorption-evaporator (1) via the second coolant pump (22) and the absorption-evaporator (1) Further, the refrigerant vapor passage is connected to the first absorption-generator (3), or is determined to be the first condenser (16) having the refrigerant liquid tube After the third throttle valve (26) is connected to the absorption-evaporator (1), the absorption-evaporator (1) is further connected to the first absorption-generator (3) through the refrigerant vapor passage, the first condenser (16) The heated medium pipe is connected to the outside, the second condenser (17) and the cooling medium pipe are connected to the outside, and the first evaporator (18) and the second evaporator (19) respectively have a residual heat medium pipe. The road is connected to the outside to form a single-stage single-effect regenerative third-class absorption heat pump; wherein: 1 when there is no second evaporator (19), the second condenser (17) has a refrigerant liquid pipeline through the first cold The liquid medium pump (21) is connected to the first evaporator (18) or the second evaporator (19) to determine that the second condenser (17) has a refrigerant liquid line through the first refrigerant liquid pump (21) and the first An evaporator (18) is connected to cancel the refrigerant liquid line of the first evaporator (18) communicating with the second evaporator (19) via the second throttle valve (24), and the first evaporator (18) is added with cold The vapor channel of the agent is connected to the second absorption-generator (4); 2 the first condenser (16) has a refrigerant liquid pipeline through the first The flow valve (20) is in communication with the first evaporator (18) and is adjusted to be a first condenser (16). The refrigerant liquid line is connected to the second evaporator (19) via the first throttle valve (20), and The first evaporator (18) has a refrigerant liquid line connected to the second evaporator (19) via the second throttle valve (24) to be adjusted to a second evaporator (19) with a refrigerant liquid line through the second section The flow valve (24) is in communication with the first evaporator (18).  8. A regenerative third type absorption heat pump, wherein the first condenser is added to the regenerative absorption-generation system in which the second absorption-generator is not connected to the outside by the heating medium line according to claim 3. a second condenser, a first evaporator, a second evaporator, a first refrigerant liquid pump, a first throttle valve, a second refrigerant liquid pump or a second throttle valve, and the generator (5) is cooled The agent vapor passage is connected to the outside to determine that the generator (5) has a refrigerant vapor passage communicating with the first condenser (16), the first condenser (16) The refrigerant liquid line is connected to the first evaporator (18) via the first throttle valve (20), and the first steam distribution chamber (11) has a refrigerant vapor passage connected to the outside to be determined as the first The steam dividing chamber (11) has a refrigerant vapor passage communicating with the second condenser (17), and the second condenser (17) and the refrigerant liquid pipeline passing through the first refrigerant liquid pump (21) and the second evaporator (19) Connect, connect the second absorption-generator (4) with refrigerant vapor passage to the outside to determine the second evaporator (19). The refrigerant vapor passage is connected to the second absorption-generator (4). The absorption-evaporator (1) has a refrigerant vapor passage communicating with the outside to determine that the first evaporator (18) has a refrigerant vapor passage communicating with the absorption-evaporator (1), and the absorber (2) has a refrigerant vapor passage The external communication is determined to be that the first evaporator (18) has a refrigerant vapor passage communicating with the absorber (2), and the external refrigerant liquid line is connected to the absorption-evaporator (1) and the absorption-evaporator (1) Further, the refrigerant vapor passage is connected to the first absorption-generator (3) to be determined as the first evaporator (18), and the refrigerant liquid pipeline is passed through the second refrigerant liquid pump (22) The absorption-evaporator (1) is connected to the absorption-evaporator (1) and then the refrigerant vapor channel is connected to the first absorption-generator (3), or is determined to be the first condenser (16) having a refrigerant liquid line After the second throttle valve (24) is connected to the absorption-evaporator (1), the absorption-evaporator (1) is cooled by a refrigerant. The claim steam passage is in communication with the first absorption-generator (3), the first condenser (16) and the heated medium line are in communication with the outside, the second condenser (17) and the cooling medium line and the exterior Connected, the first evaporator (18) and the second evaporator (19) respectively have a residual heat medium pipeline connected to the outside to form a single-stage single-effect regenerative third-type absorption heat pump; wherein: a three-way valve, the first evaporator (18) increases the refrigerant liquid line to communicate with the second evaporator (19) via the third throttle valve (25), and the second condenser (17) has a refrigerant liquid The pipeline is changed to the second condenser (17) through the first refrigerant liquid pump (21) and the second evaporator (19). The refrigerant liquid pipeline is passed through the first refrigerant liquid pump (21) and the first evaporation. (18) is connected; 2 when there is no second evaporator (19), the second condenser (17) has a refrigerant liquid line connected to the second evaporator (19) and the second evaporator (19) a refrigerant liquid line for the second condenser (17) is connected to the first evaporator (18) via the first refrigerant liquid pump (21), and the first evaporator (18) is added with a refrigerant vapor pass. The track is connected to the second absorption-generator (4).  9. A regenerative third type absorption heat pump, in the regenerative absorption-generation system according to claim 4, wherein the second absorption-generator has a medium to be heated and communicated with the outside, the first condenser is added a second condenser, a first evaporator, a second evaporator, a third evaporator, a first throttle valve, a first refrigerant liquid pump, a second throttle valve, a third throttle valve, and a second refrigerant a liquid pump or a fourth throttle valve, the generator (5) having a refrigerant vapor passage communicating with the outside is determined as a generator (5) having a refrigerant vapor passage communicating with the first condenser (16), the first condenser ( 16) There is also a refrigerant liquid line connected to the second evaporator (19) via the first throttle valve (20), and a second evaporator (19) and a refrigerant liquid line through the third throttle valve (25) ) with the first evaporator (18) communicating, the first evaporator (18) and the refrigerant liquid line are connected to the third evaporator (23) via the second throttle valve (24), and the first steam dividing chamber (11) has a refrigerant The steam passage is connected to the outside as the first steam dividing chamber (11), and the refrigerant vapor passage is connected to the second condenser (17), and the second condenser (17) and the refrigerant liquid pipeline are passed through the first refrigerant liquid. The pump (21) is in communication with the second evaporator (19), and the second absorption-generator (4) has a refrigerant vapor passage communicating with the outside to determine the second evaporator (19) having a refrigerant vapor passage and a second absorption - The generator (4) is connected, and the absorption-evaporator (1) has a refrigerant vapor passage connected to the outside to determine the third evaporator (23). The refrigerant vapor passage is connected to the absorption-evaporator (1) and will absorb Device (2) The refrigerant vapor passage is connected to the outside as the first evaporator (18). The refrigerant vapor passage is connected to the absorber (2), and the external refrigerant liquid line is connected to the absorption-evaporator (1). After the absorption-evaporator (1), the refrigerant vapor passage is connected to the first absorption-generator (3) to determine that the first evaporator (18) or the second evaporator (19) has a refrigerant liquid pipeline. The second refrigerant liquid pump (22) is connected to the absorption-evaporator (1) and the absorption-evaporator (1) is further connected to the first absorption-generator (3) or to the first condenser. (16) The refrigerant liquid pipeline is connected to the absorption-evaporator (1) via the fourth throttle valve (26), and then the absorption-evaporator (1) has a refrigerant vapor passage and a first absorption-generator (3). Connected, the first condenser (16) and the heated medium line communicate with the outside, the second condenser (17) and the cooling medium line communicate with the outside, the first evaporator (18), the second evaporator (19) and the third evaporator (23) respectively have a residual heat medium pipeline connected to the outside to form a single-stage single-effect regenerative third type absorption heat Pump; wherein: 1 can choose to connect the first condenser (16) refrigerant liquid pipeline to the second evaporator (19) via the first throttle valve (20), and the second evaporator (19) to be cold again The agent liquid pipeline is connected to the first evaporator (18) via the third throttle valve (25) to be changed into a first condenser (16) having a refrigerant liquid pipeline passing through the first throttle valve (20) and the first evaporation (18) connected, the first evaporator (18) or the third evaporator (23) has a refrigerant liquid line connected to the second evaporator (19) via the third throttle valve (25), and the second condensation (17) The refrigerant liquid line is connected to the second evaporator (19) through the first refrigerant liquid pump (21) to be changed to the second condenser (17), and the refrigerant liquid line is passed through the first coolant liquid. The pump (21) is in communication with the second evaporator (19) or the first evaporator (18); 2 when there is no second evaporator, the second condenser (17) The refrigerant liquid pipeline is connected to the second evaporator (19) via the first refrigerant liquid pump (21) to be changed to the second condenser (17), and the refrigerant liquid pipeline is passed through the first refrigerant liquid pump. (21) communicating with the first evaporator (18), the first condenser (16) having a refrigerant liquid line connected to the second evaporator (19) via the first throttle valve (20), and the second evaporator ( 19) The refrigerant liquid line is connected to the first evaporator (18) via the third throttle valve (25) to be changed to the first condenser (16). The refrigerant liquid line is passed through the first throttle valve (20). ) communicating with the first evaporator (18), the first evaporator (18) adding a refrigerant vapor channel and a second absorption-generator (4) Connected. 10. A regenerative third type absorption heat pump, wherein in the regenerative absorption-generation system in which the second absorption-generator is connected to the outside without the heated medium line, the first condenser is added Second condenser, first evaporator, first The second evaporator, the third evaporator, the first throttle valve, the first refrigerant liquid pump, the second throttle valve, the second refrigerant liquid pump or the third throttle valve, the generator (5) The refrigerant vapor passage is connected to the outside to determine that the generator (5) has a refrigerant vapor passage communicating with the first condenser (16), and the first condenser (16) and the refrigerant liquid pipeline are passed through the first throttle valve. (20) communicating with the first evaporator (18), the first evaporator (18) and the refrigerant liquid line are connected to the third evaporator (23) via the second throttle valve (24), and the first point is The steam chamber (11) has a refrigerant vapor passage communicating with the outside to determine that the first steam dividing chamber (11) has a refrigerant vapor passage communicating with the second condenser (17), and the second condenser (17) also has a refrigerant liquid The pipeline is connected to the second evaporator (19) via the first refrigerant liquid pump (21), and the second absorption-generator (4) has a refrigerant vapor passage communicating with the outside to determine the second evaporator (19). The refrigerant vapor passage is connected to the second absorption-generator (4), and the absorption-evaporator (1) has a refrigerant vapor passage connected to the outside to be determined as a third evaporator (23) A refrigerant vapor passage is connected to the absorption-evaporator (1), and the absorber (2) has a refrigerant vapor passage communicating with the outside to determine that the first evaporator (18) has a refrigerant vapor passage connected to the absorber (2). The external refrigerant liquid line is connected to the absorption-evaporator (1), and the absorption-evaporator (1) is further connected to the first absorption-generator (3) to be the first evaporator ( 18) The refrigerant liquid line is connected to the absorption-evaporator (1) via the second coolant pump (22), the absorption-evaporator (1), and the refrigerant vapor channel and the first absorption-generator (3). Connected, or determined to be the first condenser (16) with a refrigerant liquid line connected to the absorption-evaporator (1) via the third throttle valve (25), the absorption-evaporator (1) a refrigerant vapor passage is connected to the first absorption-generator (3), the first condenser (16) is further connected to the outside by the heated medium line, and the second condenser (17) has a cooling medium. The pipeline is connected to the outside, and the first evaporator (18), the second evaporator (19) and the third evaporator (23) respectively have a residual heat medium pipeline connected to the outside to form a single-stage single-effect regenerative third. An absorption type heat pump; wherein: 1 optionally adding a fourth throttle valve, the first evaporator (18) or the third evaporator (23) adding a coolant liquid line through the fourth throttle valve (26) and the second The evaporator (19) is connected, and the second condenser (17) has a refrigerant liquid pipeline connected to the second evaporator (19) through the first refrigerant liquid pump (21) to be changed into a second condenser (17). The refrigerant liquid pipeline is connected to the first evaporator (18) via the first refrigerant liquid pump (21); 2 the second condenser (17) has the refrigerant liquid pipeline when there is no second evaporator (19) The first refrigerant liquid pump (21) is connected to the second evaporator (19) to be changed to the second condenser (17) The refrigerant liquid line is connected to the first evaporator (18) via the first refrigerant liquid pump (21), and the first evaporator (18) increases the refrigerant vapor passage and the second absorption-generator (4) ) Connected.  11. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5-6, adding a new generator, a new throttle valve and a new solution heat exchange The first solution pump (6) adds a dilute solution line through the new solution heat exchanger (C) to the new generator (A), the new generator (A) and the concentrated solution line are added. The solution heat exchanger (C) is in communication with the second absorption-generator (4), and the generator (5) has a refrigerant vapor passage connected to the first condenser (16) to be adjusted to a generator (5) having a refrigerant vapor. After the channel is connected with the newly added generator (A), a new generator (A) is added, and then a refrigerant liquid line is connected to the first condenser (16) via a new throttle valve (B) - the cold released by the generator The agent steam is used as the driving heat medium of the newly added generator, and the new generator (A) and the refrigerant vapor channel are connected with the first condenser (16) to form a single-stage parallel double-effect regenerative type III absorption heat pump. .  12. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claims 7-10, adding a new generator, a new throttle valve and a new solution heat exchange The first solution pump (6) adds a dilute solution line through the new solution heat exchanger (C) to the new generator (A), and the new generator (A) and the concentrated solution line are added. The solution heat exchanger (C) is then merged with the generator (5) through the concentrated solution line after the first solution heat exchanger (9), and then passed through the second absorption-generator (4) and the first separation chamber ( 11) Connect, connect the generator (5) refrigerant vapor channel to the first condenser (16) to adjust the generator (5) with the refrigerant vapor channel and the new generator (A) to connect to the new generator (A) The refrigerant liquid line is connected to the first condenser (16) via the newly added throttle valve (B) - the refrigerant vapor released by the generator is used as the driving heat medium for the newly added generator, and the addition occurs. The device (A) also has a refrigerant vapor passage communicating with the first condenser (16) to form a single-stage parallel double-effect regenerative third-stage absorption heat pump. 13. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5-6, adding a new generator, a new throttle valve and a new solution heat exchange , the generator (5) has a concentrated solution pipeline connected to the second absorption-generator (4) through the first solution heat exchanger (9) to adjust the generator (5) has a concentrated solution pipeline through the new solution Hot Claim The exchanger (C) is connected to the newly added generator (A), and the new generator (A) and the concentrated solution line are connected to the second absorption-generator (4) via the first solution heat exchanger (9). The second absorption-generator (4) has a dilute solution line connected to the generator (5) via the first solution pump (6) and the first solution heat exchanger (9) to be adjusted to a second absorption-generator (4) The dilute solution line is connected to the generator (5) via the first solution pump (6), the first solution heat exchanger (9) and the new solution heat exchanger (C), and the generator (5) is cold The agent vapor channel is connected to the first condenser (16) and is adjusted to be a generator (5). The refrigerant vapor channel is connected with the new generator (A), and the new generator (A) is added. The throttle valve (B) is connected to the first condenser (16) - the refrigerant vapor released by the generator is used as the driving heat medium for the newly added generator, and the new generator (A) and the refrigerant vapor channel are added. A condenser (16) is connected to form a single-stage series double-effect regenerative third-stage absorption heat pump.  14. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claims 7-10, adding a new generator, a new throttle valve and a new solution heat exchange a generator solution (5) having a concentrated solution line connected to the first splitter chamber (11) via the first solution heat exchanger (9) and the second absorption generator (4) to be a generator (5) The concentrated solution pipeline is connected to the newly added generator (A) via the new solution heat exchanger (C), and the new generator (A) and the concentrated solution pipeline are passed through the first solution heat exchanger (9) and the first a second absorption-generator (4) is in communication with the first distribution chamber (11), and the second absorption-generator (4) has a dilute solution line through the first solution pump (6) and the first solution heat exchanger ( 9) Connected to the generator (5) to adjust to the second absorption-generator (4) with a dilute solution line through the first solution pump (6), the first solution heat exchanger (9) and the new solution heat exchanger (C) is in communication with the generator (5), and the generator (5) has a refrigerant vapor passage connected to the first condenser (16) to be adjusted to a generator (5) having a refrigerant vapor passage and a new After the generator (A) is connected, a new generator (A) is connected, and then a refrigerant liquid line is connected to the first condenser (16) via a new throttle valve (B) - the refrigerant vapor released by the generator is used as a new The generator heat medium is added, and the new generator (A) and the refrigerant vapor passage are connected with the first condenser (16) to form a single-stage series double-effect regenerative type third absorption heat pump.  15. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claims 13-14, wherein the second absorption-generator (4) has a dilute solution line A solution pump (6), a first solution heat exchanger (9) and a new solution heat exchanger (C) are connected to the generator (5) to be adjusted to a second absorption-generator (4) having a dilute solution line The first solution pump (6) and the first solution heat exchanger (9) are directly connected to the newly added generator (A) and then connected to the generator (5) via the new solution heat exchanger (C) to form Single-stage series-parallel double-effect regenerative third-class absorption heat pump.  16. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 5-6, adding a new generator, adding a new throttle valve, and adding a solution heat exchange. And a new solution pump, the second absorption-generator (4) has a dilute solution line connected to the first solution pump (6) and the first solution heat exchanger (9) and the generator (5) to adjust The second absorption-generator (4) has a dilute solution line connected to the new generator (A) via the first solution pump (6) and the first solution heat exchanger (9), and the new generator (A) is further The concentrated solution line is connected to the generator (5) via a new solution pump (D) and a new solution heat exchanger (C), and the generator (5) has a concentrated solution line through the first solution heat exchanger (9) Connected to the second absorption-generator (4) to adjust the generator (5) to have a concentrated solution line through the new solution heat exchanger (C) and the first solution heat exchanger (9) and the second absorption-occurrence The device (4) is connected, and the generator (5) has a refrigerant vapor channel connected to the first condenser (16) and is adjusted to be a generator (5) having a refrigerant vapor channel connected to the newly added generator (A). The new generator (A) and the refrigerant liquid line are connected to the first condenser (16) via the new throttle valve (B) - the refrigerant vapor released by the generator is used as the driving heat medium for the newly added generator. The new generator (A) and the refrigerant vapor passage are connected with the first condenser (16) to form a single-stage series double-effect regenerative third-stage absorption heat pump. 17. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 7-10, adding a new generator, adding a new throttle valve, and adding a solution heat exchange. And a new solution pump, the second absorption-generator (4) has a dilute solution line connected to the first solution pump (6) and the first solution heat exchanger (9) and the generator (5) to adjust The second absorption-generator (4) has a dilute solution line connected to the new generator (A) via the first solution pump (6) and the first solution heat exchanger (9), and the new generator (A) is further The concentrated solution line is connected to the generator (5) via a new solution pump (D) and a new solution heat exchanger (C), and the generator (5) has a concentrated solution line through the first solution heat exchanger (9) And the second absorption-generator (4) is connected to the first steam dividing chamber (11) to be adjusted to the generator (5) having a concentrated solution line through the new solution heat exchanger (C), the first solution Claim The liquid heat exchanger (9) and the second absorption-generator (4) are in communication with the first steam dividing chamber (11), and the generator (5) refrigerant vapor passage is connected to the first condenser (16) to be adjusted to The generator (5) has a refrigerant vapor passage connected to the new generator (A) and a new generator (A). The refrigerant liquid line is further added with a new throttle valve (B) and a first condenser (16). Connected - the refrigerant vapor released by the generator is used as the driving heat medium for the new generator. The new generator (A) and the refrigerant vapor channel are connected to the first condenser (16) to form a single-stage series double effect. A regenerative third type absorption heat pump.  18. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claims 16-17, wherein the second absorption-generator (4) has a dilute solution line a solution pump (6) and a first solution heat exchanger (9) are connected to the new generator (A) to be adjusted to a second absorption-generator (4) having a dilute solution line through the first solution pump (6) and The first solution heat exchanger (9) is then connected to the newly added generator (A) and the generator (5) to form a single-stage series-parallel double-effect regenerative third-class absorption heat pump.  19. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5-6, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger and the addition of the second solution heat exchanger, and the addition of the first solution pump (6) to the dilute solution pipeline respectively The solution heat exchanger (C) is connected to the newly added first generator (A) and the second solution heat exchanger (G) is added and the second generator is added. (E) connected, a new first generator (A) and a concentrated solution line are connected to the second absorption-generator (4) via a new first solution heat exchanger (C), and a second generator is added. (E) further, the concentrated solution line is connected to the second absorption-generator (4) via the newly added second solution heat exchanger (G), and the generator (5) has a refrigerant vapor passage and a first condenser ( 16) The connection is adjusted to the generator (5). The coolant flow channel is connected with the newly added first generator (A), and the first generator (A) is added, and then the refrigerant liquid pipeline is added with the first throttle. The valve (B) is in communication with the first condenser (16) - the refrigerant vapor generated by the generator is used as a driving heat medium for adding the first generator, and the first generator (A) and the refrigerant vapor channel are added. Add a second generator (E) to connect and add a second generator (E). Then the refrigerant liquid line is connected to the first condenser (16) via a new second throttle valve (F). Increasing the refrigerant vapor generated by the first generator as a driving heat medium for adding the second generator, adding a second generator (F) and a refrigerant vapor passage to communicate with the first condenser (16) , Forming a single-stage parallel three-effect regenerative third-class absorption heat pump.  20. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 7-10, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger and the addition of the second solution heat exchanger, and the addition of the first solution pump (6) to the dilute solution pipeline respectively The solution heat exchanger (C) is connected to the newly added first generator (A) and the second solution heat exchanger (G) is added and the second generator is added. (E) connected, newly added first generator (A) with concentrated solution pipeline added by new first solution heat exchanger (C) and new second generator (E) with concentrated solution pipeline added The second solution heat exchanger (G) is then merged with the generator (5) through the concentrated solution line after the first solution heat exchanger (9), and then passed through the second absorption-generator (4) and the first point. The steam chamber (11) is connected, and the generator (5) has a refrigerant vapor passage connected to the first condenser (16) and is adjusted to be a generator (5) having a refrigerant vapor passage connected to the newly added first generator (A). After the addition of the first generator (A), the refrigerant liquid line is connected to the first condenser (16) via the addition of the first throttle valve (B) - the refrigerant vapor generated by the generator is added as the new a generator driving the heat medium, adding a first generator (A) and a refrigerant vapor channel to connect with the newly added second generator (E), adding a second generator (E) and then a refrigerant liquid pipe The second throttle valve (F) is connected to the first condenser (16) by adding a new refrigerant vapor generated by the first generator as a driving heat medium for adding the second generator. The second generator (F) also has a refrigerant vapor passage communicating with the first condenser (16) to form a single-stage parallel three-effect regenerative third-stage absorption heat pump. 21. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5-6, adding a new first generator, adding a second generator, adding a first throttle valve, a second throttle valve, a first solution heat exchanger and a second solution heat exchanger are added, and the generator (5) has a concentrated solution line through the first solution heat exchanger (9) Connected to the second absorption-generator (4) to adjust to the generator (5). The concentrated solution line is connected to the newly added first generator (A) via the first solution heat exchanger (9). The first generator (A) also has a concentrated solution line, a first solution heat exchanger (C) is connected to the newly added second generator (E), a second generator (E) is added, and a concentrated solution tube is added. The second solution heat exchanger (G) is connected to the second absorption-generator (4), and the second absorption-generator (4) has a dilute solution line through the first solution pump. Claim (6) and the first solution heat exchanger (9) is connected to the generator (5) to be adjusted to a second absorption-generator (4) having a dilute solution line through the first solution pump (6), adding a second solution The heat exchanger (G), the newly added first solution heat exchanger (C) and the first solution heat exchanger (9) are in communication with the generator (5), and the generator (5) has a refrigerant vapor passage and the first The condenser (16) is connected and adjusted to the generator (5). The refrigerant vapor channel is connected with the newly added first generator (A), and the first generator (A) is added, and then the refrigerant liquid pipeline is added. The throttle valve (B) is in communication with the first condenser (16) - the refrigerant vapor generated by the generator is used as a driving heat medium for adding the first generator, and the first generator (A) and the refrigerant are added. A second generator (E) is added after the steam passage is connected to the newly added second generator (E), and the refrigerant liquid line is connected to the first condenser (16) via a new second throttle valve (F). ——Adding the refrigerant vapor generated by the first generator as the driving heat medium for adding the second generator, adding a second generator (F) There is also a refrigerant vapor passage communicating with the first condenser (16) to form a single-stage series three-effect regenerative third type absorption heat pump.  22. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 7-10, adding a new first generator, adding a second generator, adding The first throttle valve, the second section is widened, the first solution heat exchanger is added, and the second solution heat exchanger is added, and the generator (5) has a concentrated solution line through the first solution heat exchanger. (9) and the second absorption-generator (4) is connected to the first steam distribution chamber (11) to adjust the generator (5) to have a concentrated solution pipeline through the first solution heat exchanger (9) and to add a first The generator (A) is connected, the first generator (A) is added, and the first solution heat exchanger (C) is added to the new solution heat exchanger (C) to connect with the newly added second generator (E). (E) and the concentrated solution line are connected to the first steam dividing chamber (11) via the newly added second solution heat exchanger (G) and the second absorption-generator (4), and the second absorption-generator (4) The dilute solution line is connected to the generator (5) via the first solution pump (6) and the first solution heat exchanger (9) to be adjusted to a second absorption-generator (4) having a dilute solution line the first a solution pump (6), a new second solution heat exchanger (G), a new first solution heat exchanger (C), and a first solution heat exchanger (9) connected to the generator (5), the generator (5) There is a refrigerant vapor passage connected to the first condenser (16) to adjust the generator (5) to have a refrigerant vapor passage connected with the newly added first generator (A) to add a first generator (A) Then, the refrigerant liquid pipeline is connected with the first condenser (16) by adding a first section of the flow (B) - the refrigerant vapor generated by the generator is used as a driving heat medium for adding the first generator, and newly added The first generator (A) also has a refrigerant vapor passage connected to the newly added second generator (E) to add a second generator (E) and a refrigerant liquid line through the addition of a second throttle valve ( F) communicating with the first condenser (16) - adding the refrigerant vapor generated by the first generator as the driving heat medium for adding the second generator, adding the second generator (F) and the refrigerant vapor The passage is in communication with the first condenser (16) to form a single-stage series three-effect regenerative third type absorption heat pump.  23. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5-6, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger, the addition of the second solution heat exchanger, the addition of the first solution pump and the addition of the second solution pump, the second absorption -generator (4) The dilute solution line is connected to the generator (5) via the first solution pump (6) and the first solution heat exchanger (9) to be adjusted to the second absorption-generator (4) The first solution pump (6) and the first solution heat exchanger (9) are connected to the newly added second generator (E), and the second generator (E) and the concentrated solution line are added with the second solution. The pump (H) and the newly added second solution heat exchanger (G) are connected to the newly added first generator (A), the first generator (A) is added, and the concentrated solution line is added by the first solution pump. (D) and the new first solution heat exchanger (C) is connected to the generator (5), and the generator (5) has a concentrated solution line through the first solution heat exchanger (9) and the second absorption occurs. (4) Connected to generator (5) There is a concentrated solution line through the addition of the first solution heat exchanger (C), the addition of the second solution heat exchanger (G) and the first solution heat exchanger (9) ) communicating with the second absorption-generator (4), connecting the generator (5) with the refrigerant vapor passage and the first condenser (16) to adjust the generator (5) with the refrigerant vapor passage and adding the first After the generator (A) is connected, the first generator (A) is added, and then the refrigerant liquid pipeline is connected to the first condenser (16) by adding a first section of the flow (B) - the cold generated by the generator The agent steam is used as the driving heat medium for adding the first generator, and the first generator (A) is added, and the refrigerant vapor channel is connected with the newly added second generator (E) to add the second generator (E). The refrigerant liquid pipeline is connected to the first condenser (16) by adding a second throttle valve (F) - adding the refrigerant vapor generated by the first generator as the driving heat of the newly added second generator Medium, new second generator (F) There is also a refrigerant vapor passage communicating with the first condenser (16) to form a single-stage series three-effect regenerative third type absorption heat Claims pump.  24. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 7-10, adding a new first generator, adding a second generator, adding The first throttle valve, the addition of the second throttle valve, the addition of the first solution heat exchanger, the addition of the second solution heat exchanger, the addition of the first solution pump and the addition of the second solution pump, the second absorption -generator (4) The dilute solution line is connected to the generator (5) through the first solution pump (6> and the first solution heat exchanger (9) to the second absorption-generator (4) The first solution pump (6) and the first solution heat exchanger (9) are connected to the newly added second generator (E), and the second generator (E) and the concentrated solution line are added with the second solution. The pump (H) and the newly added second solution heat exchanger (G) are connected to the newly added first generator (A), the first generator (A) is added, and the concentrated solution line is added by the first solution pump. (D) and the first solution heat exchanger (C) is connected to the generator (5), and the generator (5) has a concentrated solution line through the first solution heat exchanger (9) and the second absorption occurs. The device (4) is connected to the first steam dividing chamber (11) and is adjusted to be a generator (5) having a concentrated solution pipeline, adding a first solution heat exchanger (C), and adding a second solution heat exchanger (G) The first solution heat exchanger (9) and the second absorption-generator (4) are in communication with the first steam dividing chamber (11), and the generator (5) has a refrigerant vapor passage and a first condenser (16) even Adjusted to generator (5) with refrigerant vapor channel and new first generator (A) After adding, the first generator (A) is added, and then the refrigerant liquid line is connected to the first condenser (16) via the addition of the first throttle valve (B) - the refrigerant vapor generated by the generator As the driving heat medium for adding the first generator, the first generator (A) and the refrigerant vapor channel are connected with the newly added second generator (E), and the second generator (E) is added. The refrigerant liquid pipeline is connected to the first condenser (16) by adding a second throttle valve (F) - adding the refrigerant vapor generated by the first generator as the driving heat medium for adding the second generator. A second generator (F) and a refrigerant vapor passage are connected to the first condenser (16) to form a single-stage series three-effect regenerative third-stage absorption heat pump.  25. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5, adding a new solution heat exchanger, adding an absorption-evaporator and adding a new refrigerant The liquid pump adjusts the absorption-evaporator (1) with a dilute solution line through the third solution pump (8) to the first absorption-generator (3) to adjust to the absorption-evaporator (1) The new solution heat exchanger (C) is connected to the new absorption-evaporator (I), and the new absorption-evaporator (I) and the dilute solution line are exchanged with the third solution pump (8) and the new solution. (C) is in communication with the first absorption-generator (3), and the first evaporator (18) The refrigerant vapor passage is connected to the absorption-evaporator (1) and the absorber (2) to adjust to the first evaporator (8). The refrigerant vapor passage is connected to the new absorption-evaporator (I). The first evaporator (18) or the second condenser (17) adds a refrigerant liquid line through the newly added refrigerant liquid pump (J) and the new absorption-evaporator (I) to connect the new absorption-evaporator ( I) a further refrigerant vapor channel is connected to the absorption-evaporator (1) and the absorber (2), respectively, to form a single-generator two-stage regenerative type with a new absorption-evaporator supplying refrigerant vapor to the absorber. Three types of absorption heat pumps.  26. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 7-8, adding a new refrigerant liquid pump or a new throttle valve, adding a new solution a heat exchanger and a new absorption-evaporator, the absorption-evaporator (1) having a dilute solution line is connected to the first absorption-generator (3) via the third solution pump (8) to be an absorption-evaporator ( 1) The dilute solution line is connected to the new absorption-evaporator (I) via the new solution heat exchanger (C), the new absorption-evaporator (I) and the dilute solution line are passed through the third solution pump ( 8) and the new solution heat exchanger (C) is connected to the first absorption-generator (3), and the first evaporator (18) has a refrigerant vapor channel and an absorption-evaporator (1) and an absorber ( 2) The communication is adjusted to be that the first evaporator (8) has a refrigerant vapor passage communicating with the newly added absorption-evaporator (I), and the first evaporator (18) is provided with a refrigerant liquid pipeline via the newly added refrigerant liquid pump ( J) connected with the new absorption-evaporator (I), the new absorption-evaporator (I) and then the refrigerant vapor channel are connected to the absorption-evaporator (1) and the absorber (2), respectively. The first condenser (16) adds a refrigerant liquid pipeline through the new throttle valve (B) and the new absorption-evaporator (I), and then adds an absorption-evaporator (I) and then a refrigerant vapor channel respectively. It is in communication with the absorption-evaporator (1) and the absorber (2) to form a single-stage two-stage regenerative third-stage absorption heat pump that supplies refrigerant vapor to the absorber by a new absorption-evaporator. 27. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5, adding a new solution heat exchanger, a new solution pump, and a new absorption-evaporator And adding a refrigerant liquid pump, connecting the absorber (2) with a dilute solution line and the absorption-evaporator (1) to an absorber (2) having a dilute solution line through a new solution heat exchanger (C) The claims are connected to the new absorption-evaporator (I), the new absorption-evaporator (I) and the dilute solution line via the new solution pump (D) and the new solution heat exchanger (C) and absorption. - the evaporator (1) is connected, and the refrigerant vapor channel of the first evaporator (18) is connected to the absorption-evaporator (1) and the absorber (2), respectively, and is adjusted to have a refrigerant vapor of the first evaporator (8). The passage is connected to the new absorption-evaporator (I), and the first evaporator (18) or the second condenser (17) is provided with a refrigerant liquid line via a new refrigerant liquid pump (J) and a new absorption-evaporation After the device (I) is connected, a new absorption-evaporator (I) is added, and then a refrigerant vapor channel is connected to the absorption-evaporator (1) and the absorber (2), respectively, and is formed by the new absorption-evaporator to the absorber. Single generator two-stage regenerative third type absorption heat pump for refrigerant vapor.  28. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claims 7-8, adding a new refrigerant liquid pump or a new throttle valve, adding a new solution Heat exchanger, new solution pump and new absorption-evaporator, connect the absorber (2) with dilute solution line and absorption-evaporator (1) to the absorber (2) The solution heat exchanger (C) is connected to the new absorption-evaporator (I), and the absorption-evaporator (I) and the dilute solution line are added to the new solution pump (D) and the new solution heat exchanger. (C) communicating with the absorption-evaporator (1), adjusting the first evaporator (18) refrigerant vapor passage to the absorption-evaporator (1) and the absorber (2) to adjust to the first evaporator (8) A refrigerant vapor passage is connected to the newly added absorption-evaporator (I), and the first evaporator (18) is provided with a refrigerant liquid pipeline via a newly added refrigerant liquid pump (J) and a new absorption-evaporator (Ί) After the connection, the absorption-evaporator (I) is added and then the refrigerant vapor channel is separately connected to the absorption-evaporator. (1) Connected to the absorber (2), or the first condenser (16) is added with a refrigerant liquid pipeline. After the new throttle valve (B) is connected with the new absorption-evaporator (I), the absorption is newly added. The evaporator (I) and the refrigerant vapor channel are respectively connected to the absorption-evaporator (1) and the absorber (2) to form a single-stage generator with a new generator-evaporator supplying refrigerant vapor to the absorber. Thermal third type absorption heat pump.  29. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5, adding a new solution heat exchanger, adding an absorption-evaporator, adding a new refrigerant The liquid pump and the new solution pump adjust the second solution compartment (12) with the concentrated solution line and the absorber (2) to adjust to the second steam separation chamber (12). The concentrated solution pipeline is connected to the new solution pump ( D) Connect the new solution heat exchanger (C) to the absorber (2), and the absorber (2) has a dilute solution line and an absorption-evaporator (1) Connected to the absorber (2) The dilute solution line is connected to the new absorption-evaporator (I) via the new solution heat exchanger (C), and the new absorption-evaporator (I) is added. The solution line is connected to the absorption-evaporator (1), and the first evaporator (18) has a refrigerant vapor passage connected to the absorber (2) to be adjusted to a first evaporator (18) with a refrigerant vapor passage and a new addition. The absorption-evaporator (I) is connected, and the first evaporator (18) or the second condenser (17) is provided with a refrigerant liquid line via a newly added refrigerant liquid pump (J) and a new absorption-evaporator (I) After the connection, the absorption-evaporator (I) is added, and then the refrigerant vapor channel is connected with the absorber (2) to form a single-generator two-stage regenerative type with a new absorption-evaporator supplying refrigerant vapor to the absorber. Three types of absorption heat pumps.  30. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claim 7-8, adding a new refrigerant liquid pump or adding a new throttle valve, adding a new solution a heat exchanger, a new absorption-evaporator and a new solution pump, and a second solution compartment (12) having a concentrated solution line connected to the absorber (2) to be adjusted to have a second solution in the second steam division chamber (12) The pipeline is connected to the absorber (2) via a new solution pump (D) and a new solution heat exchanger (C), and the absorber (2) has a dilute solution line connected to the absorption-evaporator (1). The absorber (2) has a dilute solution line connected to the new absorption-evaporator (I) via a new solution heat exchanger (C), a new absorption-evaporator (I) and a dilute solution line and absorption. The evaporator (1) is connected, and the first evaporator (18) has a refrigerant vapor passage connected to the absorber (2) to be adjusted to a first evaporator (18) with a refrigerant vapor passage and a new absorption-evaporator (I). Connected, the first evaporator (18) adds a refrigerant liquid line through the new refrigerant liquid pump (J) and the new absorption-evaporator U) to add an absorption-evaporator I) there is a refrigerant vapor passage communicating with the absorber (2), or the first condenser (16) is provided with a refrigerant liquid pipeline connected to the new absorption-evaporator (I) via a new throttle valve (B). After the addition of the absorption-evaporator (I), the refrigerant vapor channel is connected to the absorber (2) to form a single generator with a new absorption-evaporator to supply the refrigerant vapor to the absorber. Absorption heat pump. 31. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5, adding a new refrigerant liquid pump, a new solution heat exchanger and a new absorber , the absorption-evaporator (1) has a dilute solution line connected to the first absorption-generator (3) through the third solution pump (8) to adjust to an absorption-evaporator (1) has a dilute solution line through the third Dissolve Claim The liquid pump (8) and the new solution heat exchanger (C) are connected to the new absorber (K), the new absorber (K) and the dilute solution line are added to the new solution heat exchanger (C) and the first An absorption-generator (3) is connected, and the absorber (2) has a medium to be heated and is connected to the outside to be adjusted to a first evaporator (18) or a second condenser (17). The refrigerant pump (J) is connected to the absorber (2) and the absorber is added (2). The refrigerant vapor channel is connected to the newly added absorber (K), and the new absorber (K) is heated. The medium line communicates with the outside to form a single-stage two-stage regenerative third type absorption heat pump that supplies refrigerant vapor to the newly added absorber from the absorber.  32. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 7-8, adding a new refrigerant liquid pump or a new throttle valve, adding a new solution The heat exchanger and the newly added absorber adjust the absorption-evaporator (1) to the absorption-evaporator (1) through the third solution pump (8) and the first absorption-generator (3) The dilute solution pipeline is connected to the newly added absorber (Κ) via the third solution pump (8) and the new solution heat exchanger (C), and the new absorber (Κ) and the dilute solution pipeline are added with the new solution. The heat exchanger (C) is in communication with the first absorption-generator (3), and the absorber (2) has a heated medium line connected to the outside to be adjusted to a first evaporator (18) to add a refrigerant liquid line through the new The refrigerant pump (J) is connected to the absorber (2) and the absorber is added (2). The refrigerant vapor passage is connected to the newly added absorber (Κ), or adjusted to the first condenser (16). The refrigerant liquid pipeline is connected to the absorber (2) via a new throttle valve (Β), and then the absorber is added (2) and the refrigerant vapor passage is connected with the newly added absorber (Κ). The absorber (Κ) and the heated medium line communicate with the outside to form a single-stage two-stage regenerative third type absorption heat pump that supplies refrigerant vapor to the newly added absorber from the absorber.  33. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5, adding a new refrigerant liquid pump or a new throttle valve, and adding a solution heat exchange And a new absorber, the generator (5) has a concentrated solution line connected to the second absorption-generator (4) through the first solution heat exchanger (9) to adjust the generator (5) with a concentrated solution tube The first solution heat exchanger (9) is connected to the newly added absorber (Κ), and the new absorber (Κ) and the dilute solution line are added to the second solution through the new solution heat exchanger (C). The device (4) is connected, and the second absorption-generator (4) has a dilute solution line connected to the generator (5) through the first solution pump (6) and the first solution heat exchanger (9) to be adjusted to the second The absorption-generator (4) has a dilute solution line connected to the generator (5) via the first solution pump (6), the new solution heat exchanger (C) and the first solution heat exchanger (9), which will absorb The device (2) has a medium to be heated and is connected to the outside to be adjusted to a second evaporator (19). A refrigerant liquid line is added through the newly added refrigerant liquid pump (J) and suction. After the device (2) is connected, the absorber (2) is further connected with the newly added absorber (Κ), or is adjusted to be the first condenser (16), and the refrigerant liquid line is added with a new throttle valve ( Β) The absorber (2) is connected to the absorber (2). The refrigerant vapor channel is connected to the newly added absorber (Κ), and the new absorber (Κ) and the heated medium pipe are connected to the outside to form a single-stage two-stage regenerative third-stage absorption heat pump that supplies refrigerant vapor to the newly added absorber from the absorber; wherein, in the absence of the second evaporator, the second evaporator (19) has a refrigerant liquid line After the newly added refrigerant liquid pump (J) is connected with the absorber (2), the absorber (2) is further connected with the refrigerant vapor passage and the newly added absorber (Κ) to be changed into the first evaporator (18) with the refrigerant. The liquid pipeline is connected to the absorber (2) through the newly added refrigerant liquid pump (J), and then the absorber (2) is connected to the newly added absorber (Κ) through the refrigerant vapor passage.  34. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claim 7-8, adding a new refrigerant liquid pump or adding a new throttle valve, adding a new solution a heat exchanger and a new absorber, connecting the generator (5) concentrated solution line to the first splitter chamber (11) via the first solution heat exchanger (9) and the second absorption generator (4) Adjusted to generator (5) The concentrated solution line is connected to the new absorber (Κ) via the first solution heat exchanger (9), the new absorber (Κ) and the dilute solution line are heated by the added solution. The exchanger (C) and the second absorption-generator (4) are in communication with the first distribution chamber (11), and the second absorption-generator (4) has a dilute solution line through the first solution pump (6) and The first solution heat exchanger (9) is connected to the generator (5) to be adjusted to a second absorption-generator (4) having a dilute solution line through the first solution pump (6), and a new solution heat exchanger (C) And the first solution heat exchanger (9) is in communication with the generator (5), and the absorber (2) has a heated medium line connected to the outside to adjust to the first evaporator (18). The pipeline is connected to the absorber (2) through the newly added refrigerant pump (J), and then the absorber (2) is connected to the refrigerant vapor passage and the new absorber (Κ), or adjusted to the first condenser (16). The refrigerant liquid pipeline is connected to the absorber (2) through the addition of a new throttle valve (Β), and then the absorber (2) has a refrigerant vapor passage and a new absorber. (Κ) Connected, the new absorber (Κ) and the heated medium line communicate with the outside to form an absorber from the absorber. The claim provides a single generator two-stage regenerative third type absorption heat pump with refrigerant vapor.  35. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5, adding a new refrigerant liquid pump or a new throttle valve, adding a solution heat exchange , a new absorber and a new solution pump, and the generator (5) concentrated solution line is connected to the second absorption-generator (4) through the first solution heat exchanger (9) to be a generator (5) The concentrated solution line is connected to the second absorption-generator (4) via the first solution heat exchanger (9) and the new solution heat exchanger (C), and the second absorption-generator (4) is sparse The solution line is connected to the generator (5) via the first solution pump (6) and the first solution heat exchanger (9) to be adjusted to a second absorption-generator (4) having a dilute solution line through the first solution pump ( 6) Connect with the new solution heat exchanger (C) and the new absorber (K), add the absorber (K) and the dilute solution line through the new solution pump (D) and the first solution heat exchanger (9) Connected to the generator (5), and the absorber (2) has a medium to be heated and connected to the outside to adjust to a second evaporator (19). Add the refrigerant pipe of the pump (J) and the absorber (2) after the absorber communicates (2) The refrigerant vapor passage is connected to the newly added absorber (K), or adjusted to the first condenser (16). The refrigerant liquid pipeline is added via the new throttle valve (B) and the absorber (2). After the connection, the absorber (2) is further connected with the newly added absorber (K), and the new absorber (Κ) and the heated medium line communicate with the outside to form an absorber from the absorber. a single generator two-stage regenerative third type absorption heat pump providing refrigerant vapor; wherein, in the absence of the second evaporator, the second evaporator (19) has a refrigerant liquid line via a new refrigerant liquid pump ( J) After the absorber (2) is connected, the absorber (2) is further connected with the refrigerant vapor channel and the newly added absorber (Κ) to be changed to the first evaporator (18), and the refrigerant liquid line is added with the new refrigerant. After the liquid pump (J) is connected to the absorber (2), the absorber (2) is connected to the newly added absorber (Κ).  36. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claim 7-8, adding a new refrigerant liquid pump or a new throttle valve, adding a new solution Heat exchanger, new absorber and new solution pump, generator (5) The concentrated solution line is connected to the first steam dividing chamber (11) via the first solution heat exchanger (9) and the second absorption-generator (4) to adjust the generator (5) to have a concentrated solution line The first solution heat exchanger (9), the new solution heat exchanger (C) and the second absorption-generator (4) are in communication with the first steam dividing chamber (11), and the second absorption-generator (4) a dilute solution line is connected to the generator (5) via the first solution pump (6) and the first solution heat exchanger (9) to be adjusted to a second absorption-generator (4) having a dilute solution line through the first The solution pump (6) and the new solution heat exchanger (C) are connected to the newly added absorber (Κ), the new absorber (Κ) and the dilute solution line are added to the solution pump (D) and the first solution. The heat exchanger (9) is in communication with the generator (5), and the absorber (2) is connected to the outside by the heating medium line to be adjusted to be the first evaporator (18), and the refrigerant liquid line is added with the new refrigerant liquid. After the pump (J) is connected to the absorber (2), the absorber (2) is connected to the newly added absorber (Κ), or is adjusted to the first condenser (16). After the new throttle valve (Β) is connected to the absorber (2), the absorber (2) is connected with the refrigerant vapor passage and the new absorber (Κ), and the new absorber (Κ) is heated. The medium line communicates with the outside to form a single-stage two-stage regenerative third type absorption heat pump that supplies refrigerant vapor to the newly added absorber from the absorber.  37. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 5-10, adding a new generator, a new solution heat exchanger, and a new solution pump. And adding an absorber, connecting the generator (5) refrigerant vapor passage to the first condenser (16) to adjust the generator (5) having a refrigerant vapor passage and connecting the new absorber (Κ), adding Absorber (Κ) and dilute solution line via new solution pump (D) and new solution heat exchanger (C) with new generator (Α) Connected, new generator (Α) and concentrated solution line connected to the new absorber (Κ) via the new solution heat exchanger (C), the new generator (Α) also has refrigerant The steam passage communicates with the first condenser (16) and has a driving heat medium pipe connected to the outside, and the newly added absorber (Κ) and the heated medium pipe communicate with the outside to form a generator to provide the newly added absorber. Double generator two-stage regenerative third type absorption heat pump for refrigerant steam. 38. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 5-10, adding a new generator, a new solution heat exchanger, and a new solution pump. , Adding a new absorber, adding a new condenser and a new throttle valve, the generator (5) adds a refrigerant vapor channel to the new absorber (Κ), adding an absorber (Κ) and a dilute solution line. The new solution pump (D) and the new solution heat exchanger (C) are connected to the new generator (Α), the new generator (Α) and the concentrated solution line are added to the new solution heat exchanger (C). ) Connected with the new absorber (Κ), the new generator (Α) and the refrigerant vapor channel are connected to the new condenser (L), the new condenser (L) and the coolant line are new. Increase throttle valve (Β) and first Claim The condenser (16) is connected, the new generator (A) and the drive heat medium line are connected to the outside, and the new absorber (K) and the new condenser (L) also have the heated medium line and the outside. Connected to form a two-stage two-stage regenerative third-stage absorption heat pump that supplies refrigerant vapor to the first condenser and the newly added absorber by the generator.  39. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 5 and 7-8, adding a new generator, a new solution heat exchanger, and adding The solution pump and the newly added absorber adjust the refrigerant vapor channel of the first evaporator (18) to the absorption-evaporator (1) and the absorber (2) respectively to adjust the first evaporator (18) to have a refrigerant vapor The channel is connected to the newly added absorber (K), the new absorber (K) and the dilute solution line are added to the new solution pump (D) and the new solution heat exchanger (C) and the new generator (A). Connected, the new generator (A) and the concentrated solution line are connected to the new absorber (K) via the new solution heat exchanger (C). The new generator (A) and the refrigerant vapor channel are respectively The absorption-evaporator (1) and the absorber (2) are connected, the new generator (A) and the driving heat medium pipe are connected to the outside, and the new absorber (K) and the heated medium pipe are connected to the outside. , forming a two-stage two-stage regenerative type of double generator that supplies refrigerant vapor from the new generator to the absorber or to the absorber and the absorption-evaporator Three absorption heat pump.  40. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 39, adding a new condenser and a new throttle valve, adding a new generator (A) An additional refrigerant vapor passage is connected to the new condenser (L), and a new condenser (L) and a refrigerant liquid line are connected to the first evaporator (18) via a new throttle valve (B). Condenser (L) There is also a medium to be heated to communicate with the outside, forming a double occurrence of new refrigerant to the new condenser and absorber or to the new condenser, absorber and absorption-evaporator. Two-stage regenerative third-class absorption heat pump.  41. A regenerative third type absorption heat pump, which is a regenerative third type absorption heat pump in which the absorption-evaporator and the second absorption-generator are connected to the outside without a heated medium line according to claim 5. In addition, add a new refrigerant liquid pump or a new throttle valve, a new generator, a new solution heat exchanger, a new solution pump and a new absorber, and the generator (5) has a refrigerant vapor channel and The first condenser (16) is connected to the generator (5). The refrigerant vapor channel is connected to the newly added absorber (K), the new absorber (K) and the dilute solution line are added to the solution pump (D). ) and new solution heat exchanger (C) with new generator (A) Connected, the new generator (A) and the concentrated solution line are connected to the new absorber (K) via the new solution heat exchanger (C), and the absorber (2) has the heated medium line. Connected to the outside to adjust the second evaporator (19) to add a refrigerant liquid pipeline. After the new refrigerant liquid pump (J) is connected with the absorber (2), the absorber (2) has a refrigerant vapor channel and newly added The absorber (K) is connected or adjusted to the first condenser (16) to add a refrigerant liquid pipeline. The new throttle valve (B) is connected to the absorber (2), and the absorber (2) is further provided with a refrigerant vapor. The channel is connected to the newly added absorber (K), and the newly added generator (A) also has a refrigerant vapor channel connected to the first condenser (16) and a driving heat medium pipe connected to the outside, and an additional absorber ( K) there is also a medium to be heated and communicated with the outside to form a double-generator two-stage regenerative third-type absorption heat pump in which the absorber and the generator jointly supply refrigerant vapor to the newly added absorber; In the case of the second evaporator, the second evaporator (19) is added with a refrigerant liquid line through the newly added refrigerant liquid pump (J) and the absorber (2) After the absorber (2), the refrigerant vapor passage is connected with the newly added absorber (K) to be changed to the first evaporator (18). The refrigerant liquid pipeline is added through the newly added refrigerant liquid pump (J) and the absorber. (2) After the connected absorber (2), the refrigerant vapor passage is connected to the newly added absorber (K).  42. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump in which the absorption-evaporator is not connected to the outside by the heating medium line, and the additional refrigerant is added. Liquid pump or new throttle valve, new generator, new solution heat exchanger, new solution pump and new absorber, the generator (5) has a refrigerant vapor channel and a first condenser (16) Connected adjustment to generator (5) with refrigerant vapor channel connected to new absorber (K), new absorber (K) and dilute solution line via new solution pump (D) and new The solution heat exchanger (C) is connected to the new generator (A), and the new generator (A) and the concentrated solution line are connected to the newly added absorber (K) via the new solution heat exchanger (C). Adjusting the absorber (2) with the heated medium line to the outside to adjust to the first evaporator (18) Adding the refrigerant liquid line through the new refrigerant liquid pump (J) and the absorber (2) after the absorber (2) The refrigerant vapor passage is connected to the newly added absorber (K), or is adjusted to the first condenser (16). The refrigerant liquid pipeline is connected with the new throttle valve (B) and the absorber (2). After the communication, the absorber (2) has a refrigerant vapor passage communicating with the newly added absorber (K), and the newly added generator (A) also has a refrigerant vapor passage connected to the first condenser (16) and having driving heat. The medium pipe is connected to the outside, and the new absorber (K) and the heated medium pipe are connected to the outside. The claim is a two-stage two-stage regenerative third-stage absorption heat pump in which the absorber and the generator jointly supply refrigerant vapor to the newly added absorber.  43. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 5, adding a new refrigerant liquid pump, a new generator, and a new solution heat exchanger a new solution pump and a new absorption-evaporator, and the first evaporator (18) has a refrigerant vapor channel connected to the absorption-evaporator (1) and the absorber (2) to be adjusted into a first evaporator. (18) The refrigerant vapor channel is connected to the new absorption-evaporator (I), the new absorption-evaporator (I) and the dilute solution pipeline are added to the new solution pump (D) and the new solution heat exchanger. (C) Connected to the new generator (A), the new generator (A) and the concentrated solution line are connected to the new absorption-evaporator (I) via the new solution heat exchanger (C). The evaporator (18) or the second condenser (17) adds a refrigerant liquid line through the newly added refrigerant liquid pump (J) and the new absorption-evaporator (I) to connect the new absorption-evaporator (I) Further, the refrigerant vapor passages are respectively connected to the absorber (2) and the absorption-evaporator (1), and the new generator (A) and the refrigerant vapor passage are respectively associated with the absorption-evaporator (1) and the absorber (2). Connected, the new generator (A) also has a drive heat medium line that communicates with the outside, forming a new absorption-evaporator and a new generator to provide the cold to the absorber or to the absorber and the absorption-evaporator together. Double-generator two-stage regenerative third-class absorption heat pump with steam.  44. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 7-8, adding a new refrigerant liquid pump or a new throttle valve, newly occurring a new solution heat exchanger, a new absorption-evaporator and a new solution pump, and the first evaporator (18) has a refrigerant vapor channel connected to the absorption-evaporator (1) and the absorber (2), respectively. Adjusted to the first evaporator (18) with a refrigerant vapor channel connected to the new absorption-evaporator (I), a new absorption-evaporator (I) and a dilute solution line via a new solution pump (D) and The new solution heat exchanger (C) is connected to the new generator (A), the new generator (A) and the concentrated solution line are added to the new solution heat exchanger (C) and the new absorption-evaporator ( I) Connected, the first condenser (16) is added with a refrigerant liquid line. After the new throttle valve (B) is connected with the new absorption-evaporator (I), the new absorption-evaporator (I) is added. The vapor channel of the agent is connected to the absorber (2) and the absorption-evaporator (1), respectively, or the first evaporator (18) Adding refrigerant liquid pipeline through the new refrigerant liquid pump (J) and adding the new absorption-evaporator (I), adding the absorption-evaporator (I) and then the refrigerant vapor channel and the absorber respectively (2) Connected to the absorption-evaporator (1), the new generator (A) and the refrigerant vapor channel are connected to the absorption-evaporator (1) and the absorber (2) respectively, and the new generator (A) is added. There is also a drive heat medium line that communicates with the outside to form a two-stage two-stage heat recovery by adding a new absorption-evaporator and a new generator to the absorber or a refrigerant generator that supplies refrigerant vapor to the absorber and the absorption-evaporator. The third type of absorption heat pump.  45. The regenerative third type absorption heat pump is the regenerative third type absorption heat pump according to claim 41, adding a new condenser and adding a new throttle valve, and adding a new generator (A There is a refrigerant vapor passage connected to the first condenser (16) to adjust to a new generator (A) with a refrigerant vapor passage communicating with the new condenser (L), adding a condenser (L) and a refrigerant The liquid pipeline is connected to the first condenser (16) via a new throttle valve (B), and the generator (5) and the absorber (2) respectively add a refrigerant vapor passage to communicate with the first condenser (16), The increasing condenser (L) and the heated medium line communicate with the outside to form a double generator two-stage regenerative type in which the absorber and the generator respectively supply the refrigerant vapor to the first condenser and the newly added absorber. Three types of absorption heat pumps.  46. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 42, adding a new condenser and adding a second throttle valve, and adding a new generator (A) The refrigerant vapor passage is connected to the first condenser (16) to adjust to the new generator (A). The refrigerant vapor passage is connected to the new condenser (L), and the new condenser (L) is added. The refrigerant liquid pipeline is connected to the first condenser (16) by adding a second throttle valve (F), and the refrigerant vapor passage and the first condenser are respectively added to the generator (5) and the absorber (2) (16) Connected, the new condenser (L) and the heated medium line communicate with the outside to form a two-stage generator with two generators that provide refrigerant vapor to the first condenser and the new absorber, respectively, by the absorber and the generator. A regenerative third type absorption heat pump. 47. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 11-18, adding a new condenser and adding a second throttle valve, the generator ( 5) Adding a refrigerant vapor channel to the new condenser α), adding a new condenser (L) and a coolant line to the first condenser (16) via a new second section (F) , the new condenser (L) and the heated medium pipeline are connected to the outside to form a single with a new condenser as the additional high-temperature heating end. The claim requires a book-level double-effect regenerative third-class absorption heat pump.  48. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 19-24, adding a new condenser and adding a third throttle valve, the generator ( 5) Adding a refrigerant vapor channel to the new condenser (L), adding a new condenser (L) and a coolant line to the first condenser (16) via a new third throttle valve. The increasing condenser (L) and the heated medium line communicate with the outside to form a single-stage three-effect regenerative third-type absorption heat pump with a new high-temperature heating end.  49. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 19-24, adding a new condenser and adding a third throttle valve, adding a new A generator (Α) additional refrigerant vapor passage is connected to the new condenser (L), and a new condenser (L) and a refrigerant liquid pipeline are added through the third throttle valve and the first condenser (16). Connected, the new condenser (L) and the heated medium line communicate with the outside to form a single-stage three-effect regenerative third-type absorption heat pump with a new high-temperature heating end.  50. The regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 47-49, wherein a new first flow regulating valve and a second second flow regulating valve are added. The first condenser (16) has a heated medium line connected to the outside to be adjusted to be externally connected to the first condenser (16) after the heated medium line is in communication with the first condenser (16). The newly added first flow throttle valve (Ν) is connected to the outside and the second flow regulating valve (0) is connected to the newly added condenser (L), and the new condenser (L) is heated. The pipeline is connected to the outside to adjust to the first condenser (16). The heated medium pipeline is connected to the new condenser (L) by adding a second flow throttle valve (0), and then the new condenser (L) is added. The heated medium line communicates with the outside to form an adjustable type of regenerative third type absorption heat pump.  51. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 11-18, adding a new second generator, adding a new absorber, and adding a new solution pump. And a new solution heat exchanger, the first new generator (Α) has a refrigerant vapor channel connected to the first condenser (16) and is adjusted to add a first generator (Α) with a refrigerant vapor channel and a new The absorber (Κ) is connected, the new absorber (Κ) and the dilute solution line are connected to the newly added second generator (Ε) via the new solution pump (D) and the new solution heat exchanger (C). , a new second generator (Ε) and a concentrated solution line are connected to the newly added absorber (Κ) via a new solution heat exchanger (C), and a second generator (Ε) is additionally provided with a refrigerant. The steam passage communicates with the first condenser (16) and has a driving heat medium pipeline connected to the outside, and the newly added absorber (Κ) and the heated medium pipeline communicate with the outside to form a single stage double effect as the first stage. The two-stage regenerative third-class absorption heat pump.  52. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 51, adding a second second throttle valve, and adding a second generator (Ε) The medium to be heated is connected to the outside to adjust to the generator (5). The refrigerant vapor channel is added and the second generator (Ε) is connected, and the second generator (Ε) is added. A second throttle valve (F) is added to communicate with the first condenser (16) - the refrigerant vapor released by the generator acts as a driving heat medium for adding the second generator, forming a single stage double effect as the first stage The two-stage regenerative third-class absorption heat pump.  53. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 11-18, adding a second addition generator, a new absorber, and a new solution pump. New solution heat exchanger, new condenser and new second throttle valve, new first generator (Α) added refrigerant vapor channel and new absorber (Κ), new absorber ( Κ) There is also a dilute solution line connected to the newly added second generator (Ε) via the new solution pump (D) and the new solution heat exchanger (C), and a second generator (Ε) is added. The solution line is connected to the newly added absorber (Κ) via the new solution heat exchanger (C), and the second generator (Ε) is added with a refrigerant vapor channel and a new condenser (U connected and driven). The heat medium pipeline is connected to the outside, and the new condenser (L) and the refrigerant liquid pipeline are connected to the first condenser (16) by adding a second throttle valve (F), and an absorber (新增) is newly added. And the newly added condenser (L) also has a heated medium pipe connected to the outside to form a two-stage regenerative with a single-stage double effect as the first stage. The third type of absorption heat pump. 54. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 53, wherein a third throttle valve is added, and a second generator (Ε) is added. The medium to be heated is connected to the outside to adjust to the generator (5). The refrigerant vapor channel is added and the second generator (Ε) is connected, and the second generator (Ε) is added. New third throttle valve (Μ) is connected to the new condenser (L) - the refrigerant vapor released by the generator is added as the second generator The driving heat medium of the claim forms a two-stage regenerative third type absorption heat pump with a single stage double effect as the first stage.  55. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claims 19-24, adding a new third generator, adding a new absorber, adding a new solution pump And a new solution heat exchanger, the second generator (E) has a refrigerant vapor passage connected to the first condenser (16) to be adjusted to add a second generator (E) with a refrigerant vapor passage and a new The absorber (K) is connected, the new absorber (K) and the dilute solution line are connected to the newly added third generator via the new solution pump (D) and the new solution heat exchanger (C). The third generator also has a concentrated solution pipeline through a new solution heat exchanger (C) Connected to the newly added absorber (K), the new third generator also has a refrigerant vapor channel connected to the first condenser (16) and a driving heat medium pipe connected to the outside, and an additional absorber (K) There is also a medium to be heated and communicated with the outside to form a two-stage regenerative third type absorption heat pump having a single-stage three-effect first stage.  56. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 55, adding a new third throttle valve, and adding a new third generator to be heated The medium pipe is connected to the outside to adjust to the generator (5) or the newly added first generator (A) is added with a refrigerant vapor channel and is connected with the newly added third generator to add a third generator and then a refrigerant liquid pipeline. The third throttle valve is connected to the first condenser (16) - the generator (5) or the new refrigerant generated by the first generator (A) is used as the driving heat medium for the newly added third generator. A two-stage regenerative third-class absorption heat pump with a single-stage three-effect first stage is formed.  57. A regenerative third type absorption heat pump is a regenerative third type absorption heat pump according to claims 19-24, adding a new third generator, a new absorber, and a new solution pump. New solution heat exchanger, new condenser and new third throttle valve, new second generator (E) additional refrigerant vapor channel connected with new absorber (K), new absorber ( K) There is also a dilute solution pipeline connected to the newly added third generator via a new solution pump (D) and a new solution heat exchanger (C), and a new third generator and a concentrated solution pipeline are added. The solution heat exchanger (C) is connected to the newly added absorber (K), and the newly added third generator also has a refrigerant vapor channel connected to the newly added condenser (L) and a driving heat medium pipe connected to the outside. The new condenser (L) and the refrigerant liquid line are connected to the first condenser (16) via the addition of the third section of the flow (M), and the new absorber (K) and the new condenser (L) are added. There is also a medium to be heated to communicate with the outside to form a two-stage regenerative third-class absorption with a single-stage three-effect first stage. Heat pump.  58. A regenerative third type absorption heat pump, in the regenerative third type absorption heat pump according to claim 57, adding a new fourth throttle valve, and adding a new third generator to be heated The medium pipe is connected to the outside to adjust to the generator (5) or the new first generator (A) is added with a refrigerant vapor channel and the third generator is connected to the new third generator and then the refrigerant liquid pipeline The fourth throttle valve is connected to the first condenser (16) - the generator (5) or the new refrigerant generated by the first generator (A) is used as the driving heat medium for the newly added third generator. A two-stage regenerative third-class absorption heat pump with a single-stage three-effect first stage is formed.