WO2004010060A1 - Refrigerating cycle - Google Patents
Refrigerating cycle Download PDFInfo
- Publication number
- WO2004010060A1 WO2004010060A1 PCT/JP2003/009319 JP0309319W WO2004010060A1 WO 2004010060 A1 WO2004010060 A1 WO 2004010060A1 JP 0309319 W JP0309319 W JP 0309319W WO 2004010060 A1 WO2004010060 A1 WO 2004010060A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- refrigerant
- evaporator
- refrigeration cycle
- temperature
- adjustment container
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B45/00—Arrangements for charging or discharging refrigerant
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/06—Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
- F25B2309/061—Compression machines, plants or systems characterised by the refrigerant being carbon dioxide with cycle highest pressure above the supercritical pressure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/047—Water-cooled condensers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/01—Heaters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/16—Receivers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2106—Temperatures of fresh outdoor air
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B40/00—Subcoolers, desuperheaters or superheaters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
- F25B9/008—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
Definitions
- the present invention relates to a refrigeration cycle, for example, a refrigeration cycle that can be used for a heat source unit of a heat pump water heater.
- the heat pump water heater generally includes a tank unit 51 having a hot water storage tank 50 and a heat source unit 53 having a refrigeration cycle 52.
- the refrigeration cycle 52 is configured by connecting a compressor 54, a water heat exchanger (condenser) 55, an expansion valve 57, and an evaporator 58 in this order.
- the tank unit 51 includes the hot water storage tank 50 and a circulation path 59, and a water circulation pump 60 and a heat exchange path 61 are interposed in the circulation path 59.
- the heat exchange path 61 is constituted by a water heat exchanger 55.
- the stored water flows out from the intake port provided at the bottom of the hot water storage tank 50 into the circulation path 59. This flows through the heat exchange path 61. At this time, the hot water is heated (boiled) by the water heat exchanger 55 and returned to the upper portion of the hot water storage tank 50 from the hot water inlet. With this, high-temperature hot water is stored in the hot water storage tank 50.
- refrigerants such as dichlorodifluoromethane (R-12) and chlorodifluoromethane (R-22) have been used as refrigerants in the refrigeration cycle.
- R-134a 1,1,1,1,2-tetrahydrofluoretane
- R_134a still has problems such as high global warming ability.
- a supercritical refrigerant such as carbon dioxide is useful as the natural refrigerant.
- changes in the outside air temperature cause load fluctuations on the water heat exchanger (gas cooler) side and the evaporator side, and the amount of circulated refrigerant differs every season. That is, as shown in Fig.
- a refrigerant regulating container 65 is provided on the high pressure side, and a flow regulating valve is provided.
- the amount of refrigerant in the refrigerant adjustment container (receiver) 65 may be increased or decreased to obtain a refrigerant circulation amount according to the outside air temperature.
- a bypass circuit 67 is provided which branches off at a position downstream of the branch portion, and the receiver 65 is provided in the bypass circuit 67.
- a flow control valve 66 is provided at the outlet side of 65. That is, the bypass circuit 67 includes a first passage 68 branched from the upstream side of the water heat exchanger 55 and connected to the receiver 65, and a first passage 68 derived from the receiver 65. And a second passage 69 that joins the gas cooler 55 at a downstream side of the branching part of the second passage.
- the above-mentioned regulating valve 66 is interposed in the second passage 69.
- a refrigerant passage 70 connecting the expansion valve 57 and the evaporator 58 passes through the inside of the receiver 65.
- heat exchange is performed between the high-pressure refrigerant flowing into the receiver 65 via the bypass circuit 67 and the low-pressure refrigerant flowing through the refrigerant passage 70. Then, by adjusting the opening degree of the adjusting valve 66, the flow rate of the refrigerant passing through the receiver 65 is adjusted, and the temperature of the refrigerant in the receiver 65 is adjusted. In other words, by controlling the opening degree of the flow control valve 66, the required refrigerant temperature can be maintained, and the receiver 65 ⁇ can have an appropriate refrigerant capacity, and the refrigerant circulation amount in this circuit can be reduced. The optimal amount can be used.
- the present invention has been made in order to solve the above-mentioned conventional drawbacks.
- the purpose of the present invention is to provide a refrigerant circulation amount according to each season, thereby avoiding overheating operation and wet operation.
- Another object of the present invention is to provide a refrigeration cycle that can be configured at low cost without using a flow control valve or the like.
- a refrigeration cycle of the present invention is a refrigeration cycle in which refrigerant discharged from a compressor is returned to the compressor through a gas cooler, a decompression mechanism, and an evaporator in order.
- the refrigerant adjustment container is connected to a refrigerant passage between the container and the refrigerant via a connection passage, and the refrigerant adjustment container is arranged in a temperature environment that changes depending on the outside air temperature.
- the refrigerant passage between the decompression mechanism and the evaporator and the refrigerant adjustment container are connected via the connection passage, so that the inside of the refrigerant adjustment container is provided between the decompression mechanism and the evaporator.
- Refrigerant gas refrigerant
- the refrigerant adjustment container is placed in a temperature environment that changes depending on the outside air temperature. Therefore, for example, since the outside air is hot in summer, the refrigerant adjustment container is kept at a high temperature side, the amount of refrigerant stored in the refrigerant adjustment container decreases, and the refrigerant circulation amount in the circulation path of the refrigeration cycle decreases. Can be added.
- the refrigerant adjustment container since the outside air is cold in winter, the refrigerant adjustment container is kept at a low temperature, the amount of refrigerant stored in the refrigerant adjustment container increases, and the amount of refrigerant circulating in the circulation path of the refrigeration cycle is reduced. Can be done. That is, by placing the refrigerant adjustment container in a temperature environment that changes depending on the outside air temperature, the amount of refrigerant stored in the refrigerant adjustment container can be increased or decreased to achieve a refrigerant circulation amount according to the outside air temperature. Monkey
- the refrigerant can be circulated with the amount of refrigerant corresponding to each season, and it is possible to prevent an excessive overheating operation or a wet operation.
- the amount of circulating refrigerant varies depending on the outside air temperature without providing a bypass circuit or the like in which a regulating valve is interposed. Can be adjusted according to the temperature environment.
- the refrigeration cycle of one embodiment is characterized in that the temperature environment that changes depending on the outside air temperature is formed by a refrigerant ranging from the evaporator outlet to the compressor inlet.
- the refrigerant ranging from the evaporator outlet to the compressor inlet changes according to the outside air temperature. Therefore, a temperature environment that changes depending on the outside air temperature can be stably formed by the refrigerant, and the amount of the circulated refrigerant corresponding to the outside air temperature can be ensured.
- the refrigerant adjustment container is attached to a refrigerant pipe extending from the evaporator outlet to the compressor suction port, and the refrigerant in the refrigerant pipe and the refrigerant in the refrigerant adjustment container are heated. It is characterized by being exchanged.
- the refrigerant adjustment container is attached to the refrigerant pipe extending from the evaporator outlet to the compressor intake, the reliability of heat exchange between the refrigerant in the refrigerant pipe and the refrigerant in the refrigerant adjustment container is reduced.
- the refrigerant circulation rate is high, and the refrigerant circulation amount can be stably set according to the outside air temperature.
- the refrigeration cycle of one embodiment is characterized in that, in a refrigerant passage between the decompression mechanism and the evaporator, a throttle is provided on the evaporator side from a connection portion of the connection passage.
- the refrigeration cycle of one embodiment is characterized in that the refrigerant adjustment container is arranged so as to be exposed to the outside air.
- the refrigerant in the refrigerant adjustment container is warmed or cooled by the outside air.
- the amount of refrigerant in the refrigerant adjustment container increases and decreases according to the outside air temperature, and the amount of refrigerant circulated according to each season.
- the refrigeration cycle of one embodiment is characterized in that the refrigerant adjustment container is arranged in an air passage formed by a fan attached to the evaporator.
- the refrigerant adjustment container is provided with a fan attached to the evaporator.
- the temperature of the refrigerant adjustment container can be adjusted by this wind, since it is arranged in the wind passage generated by the above.
- the refrigeration cycle is characterized in that the refrigerant adjustment container is arranged on the leeward side downstream of the evaporator.
- the refrigerant adjustment container is arranged downstream of the evaporator on the leeward side, which is preferable in terms of heat exchange, and the temperature of the refrigerant adjustment container can be surely adjusted.
- the refrigeration cycle of one embodiment is characterized in that the temperature environment that changes depending on the outside air temperature is configured by heating or cooling the refrigerant adjustment container with a Peltier element or the like.
- the refrigerant adjustment container can be heated or cooled by a Peltier element or the like, so that the refrigerant in the refrigerant adjustment container can be reliably increased or decreased according to the outside air temperature.
- the refrigerant circulation amount can be adjusted stably according to the season.
- the refrigeration cycle of one embodiment is characterized in that the refrigerant adjustment container is arranged to exchange heat with water whose temperature changes depending on the outside air temperature.
- the temperature of the refrigerant adjustment container is adjusted by water whose temperature depends on the outside air. That is, the amount of refrigerant in the refrigerant adjustment container increases and decreases according to the outside air temperature, and the amount of refrigerant circulated according to each season.
- a refrigeration cycle includes a refrigerant passage between the decompression mechanism and the evaporator, wherein a throttle is provided on the evaporator side of a connection portion of the connection passage, and a refrigerant in the refrigerant adjustment container is provided. And heat exchange between the refrigerant and the refrigerant in the vicinity of the inlet of the evaporator on the downstream side of the throttle. Further, the refrigerant adjustment container is provided with a heater H for adjusting the amount of refrigerant.
- the refrigerant in the refrigerant adjustment container exchanges heat with the low-temperature refrigerant immediately after passing through the throttle, so that the heat exchange can be reliably performed. Since a heater for adjusting the amount of refrigerant is provided, the temperature of the refrigerant adjustment container can be adjusted according to the outside air temperature by the heater.
- the refrigeration cycle of one embodiment is characterized in that the high pressure side operates at supercritical pressure. ing.
- FIG. 1 is a simplified diagram showing an embodiment of the refrigeration cycle of the present invention.
- FIG. 2 is a Mollier diagram of the refrigeration cycle.
- FIG. 3 is a Mollier diagram of a conventional refrigeration cycle.
- FIG. 4 is a simplified view of a main part showing another embodiment of the refrigeration cycle of the present invention.
- FIG. 5 is a simplified diagram showing a comparative example of a refrigeration cycle.
- FIG. 6 is a simplified diagram of a conventional refrigeration cycle. BEST MODE FOR CARRYING OUT THE INVENTION
- FIG. 1 shows a simplified diagram of a heat pump water heater using this refrigeration cycle.
- This heat pump water heater has a tank unit 1 and a heat source unit 2, and heats water (hot water) in tank unit 1 with heat source unit 2. Is what you do.
- the tank unit 1 has a hot water storage tank 3, and the hot water stored in the hot water storage tank 3 is supplied to a bathtub or the like (not shown). That is, the hot water storage tank 3 is provided with a water supply port 5 on a bottom wall thereof and a tap hole 6 on an upper wall thereof.
- the hot water storage tank 3 has a water inlet 7 at the bottom wall and a hot water inlet 8 at the top of the side wall (peripheral wall), and the water inlet 7 and the hot water inlet 8 pass through the circulation path 9.
- the circulation path 9 is provided with a water circulation pump 10 and a heat exchange path 11.
- the heat source unit 2 includes the refrigeration cycle R according to this embodiment.
- the freezing cycle R consists of a compressor 15, a water heat exchanger (gas cooler) 16, which constitutes the heat exchange path 11, a pressure reducing mechanism (electric expansion valve) 17, and an air heat exchanger (evaporator). 1) and 8 are connected in order. That is, the discharge port of the compressor 15 and the gas cooler 16 are connected through the refrigerant passage 20, the gas cooler 16 and the electric expansion valve 1 are connected through the refrigerant passage 21, The expansion valve 17 and the evaporator 18 are connected by a refrigerant passage 22, and the evaporator 18 and the compressor 15 are connected by a refrigerant passage 24 provided with an accumulator 23.
- the refrigerant for example, carbon dioxide gas (C 0 2 ) whose high pressure side is used at a supercritical pressure is used.
- the gas cooler as the water heat exchanger 16 has a function of cooling the high-temperature and high-pressure supercritical refrigerant compressed by the compressor 15.
- the refrigerant passage 20 is provided with an HPS 25 as a pressure protection switch and a pressure sensor 26. Further, the evaporator 18 is provided with a fan 40 for adjusting the capacity.
- the refrigeration cycle R includes a liquid-gas heat exchanger 27 for cooling the high-pressure refrigerant flowing out of the gas cooler 16.
- the liquid-gas heat exchanger 27 has, for example, a double-pipe structure, in which a first passage 28 through which the refrigerant from the gas cooler 16 passes, and a refrigerant from the evaporator 18.
- a second passage 29 passing therethrough That is, the first passage 28 constitutes a part of the refrigerant passage 21 connecting the gas cooler 16 and the electric expansion valve 17, and the second passage 29 constitutes the evaporator 18 and the compressor 1.
- a part of the refrigerant passage 24 that connects to the refrigerant passage 5 is formed.
- the refrigerant adjustment container 30 is a refrigerant pipe extending from the outlet of the evaporator to the inlet of the compressor, and more specifically, the liquid gas heat exchanger 2. 7 between the second passage 29 and the accumulator 23). Therefore, the refrigerant adjustment container 30 comes into contact with the refrigerant passage 24, and heat exchange between the refrigerant in the refrigerant adjustment container 30 and the refrigerant in the refrigerant passage 24 is enabled.
- a connection passage 31 is connected to the refrigerant adjustment container 30. That is, the connection passage 3] is connected to the refrigerant passage 22 (a refrigerant passage between the pressure reducing mechanism 17 and the evaporator 18), It connects the container 30.
- the refrigerant (gas refrigerant) of the refrigeration cycle R is drawn out from between the decompression mechanism 17 and the evaporator 18 and stored in the refrigerant adjustment container 30 as a liquid refrigerant.
- the capacity of the refrigerant adjustment container 30 is determined by the cycle (compressor 15 ⁇ gas cooler 16 ⁇ decompression mechanism 17 ⁇ evaporator 18 ⁇ compressor 15 ⁇ circulation path through which the refrigerant circulates) About 1/10 of the total capacity (for example, about 300 to 400 cc).
- a throttle 33 is provided on the evaporator 18 side from the connection portion 32 (point A) of the connection passage 31.
- a force capable of using a fixed throttle such as a capillary tube or the like can be used as well as an electric expansion valve or the like.
- a throttle having a suction superheat of 3 to 5 ° C is selected. Is preferred.
- this heat pump water heater has a temperature sensor (input water thermistor) 34 that detects the temperature of the circulation path 9 on the upstream side of the heat exchange path 11, and the temperature sensor on the downstream side of the heat exchange path 11 of the circulation path 9.
- Temperature sensor (outlet hot water thermistor) 35 that detects the temperature
- temperature sensor (air heat exchange thermistor) 36 that detects the temperature of the evaporator 18, temperature sensor (the discharge pipe) that detects the discharge temperature of the compressor 15 Thermistor) 37
- a temperature sensor (outside air temperature thermistor) 38 that detects the outside air temperature are provided. Then, data (detected temperature) from these sensors is input to a control unit (not shown) (not shown) of the heat pump water heater, and various controls are performed based on the data. Done.
- the temperature of the discharge pipe is detected by the discharge pipe thermistor 37, and the opening of the electric expansion valve 17 is adjusted so that the discharge pipe temperature becomes the target discharge pipe temperature. It can be adjusted (controlled). If the temperature of the water input thermistor 34 is equal to or higher than a predetermined temperature (for example, 60 ° C.), it is determined that the hot water in the hot water storage tank 3 is boiling, and the operation is stopped. Based on the temperature, the operating frequency of the compressor 15 can be controlled to adjust the hot water heating capacity (boiling capacity) and the like.
- a predetermined temperature for example, 60 ° C.
- the compressor 15 is driven and the water circulation pump 10 is driven (operated). Then, the stored water (hot water) flows out of the water intake port 7 provided at the bottom of the hot water storage tank 3 and flows through the heat exchange path 11 of the circulation path 9. Further, the refrigerant discharged from the compressor 15 is returned to the compressor 15 via the gas cooler 16, the pressure reducing mechanism 17, and the evaporator 18 in order. Therefore, the water flowing through the heat exchange path 11 of the circulation path 9 is heated (boiled) by the water heat exchanger which is the gas cooler 16, and is returned from the hot water inlet 8 to the upper part of the hot water storage tank 3. You.
- hot water is stored in the hot water storage tank 3.
- the unit price of electricity at night is set lower than that of daytime, so it is preferable to perform this operation during the late night hours when the cost is low to reduce costs.
- the Mollier diagram for this operation is shown in Figure 2. That is, in this refrigeration cycle, the high-pressure refrigerant in the state 1 is discharged from the compressor 15 and the high-pressure refrigerant is introduced into the gas cooler 16 (water heat exchanger). The gas cooler 16 exchanges heat with water passing through the heat exchange path 11. As a result, the water passing through the heat exchange path 11 is heated (boiled). Then, due to this heat exchange, the high-pressure refrigerant radiates heat to the water, and its enthalpy drops from 1 to 2. The high-pressure refrigerant in these two states is sent to the low-pressure mechanism 17 (expansion valve).
- the high-pressure refrigerant is depressurized to the point A by the pressure reducing mechanism 17, and further reduced to the state of 3 by the throttle 33. Then, the low-pressure refrigerant is introduced into the evaporator 18. In the evaporator 18, the low-pressure refrigerant exchanges heat with air. Due to this heat exchange, the low-pressure refrigerant absorbs heat and evaporates. That is, the enthalpy increases from 3 to 4, and the low-pressure refrigerant in this 4 state is sent to the compressor 15.
- the refrigerant at the connection point 32 (point A) of the refrigerant passage 22 between the pressure reducing mechanism 17 and the evaporator 18 and the connection passage 31 flows from the evaporator outlet to the compressor inlet. And heat is exchanged with the refrigerant between the second passage 29 of the liquid-gas heat exchanger 27 and the accumulator 23 (point B). For this reason, if the temperature at the point B rises in accordance with the outside air, the temperature of the refrigerant regulating container 30 also rises, and the refrigerant storage amount decreases, and the temperature at the point B rises in accordance with the outside air. If the temperature decreases, the temperature in the refrigerant adjustment container 30 also decreases, and the amount of stored refrigerant increases.
- the refrigerant pipe (refrigerant passage 24) from the evaporator outlet to the compressor inlet is affected by the outside air temperature, and in summer when the outside air temperature is high, it is higher than in winter when the outside air temperature is low. is there. Therefore, as shown in Fig. 3, when the outside air temperature is high (high outside air), a cycle like I occurs, and when the outside air temperature is low (low outside air temperature), a cycle like ⁇ ⁇ ⁇ occurs. At the time of temperature), the density inside the evaporator 18 is higher than in winter (at low outside temperature). Therefore, there is a large difference in the amount of refrigerant in the evaporator 18 between the high outside temperature and the low outside temperature. And the amount of circulating refrigerant was large at low outside air temperatures, despite the small amount of circulating refrigerant.
- the refrigerant adjustment container 30 since the outside air has a high temperature in summer, the refrigerant adjustment container 30 is kept on the high temperature side and stored in the refrigerant adjustment container 30. As a result, the amount of refrigerant to be cooled is reduced, and the amount of refrigerant circulated in the circulation path of the refrigeration cycle can be increased. In winter, since the outside air is at a low temperature, the refrigerant adjustment container 30 is kept at a low temperature, the amount of refrigerant stored in the refrigerant adjustment container 30 increases, and the refrigerant circulation amount in the circulation path of the refrigeration cycle. Can be reduced.
- the amount of refrigerant in the refrigerant adjustment container 30 is increased or decreased to obtain a refrigerant circulation amount according to the outside air temperature. be able to. For this reason, it is possible to circulate the refrigerant with the amount of refrigerant according to each season, and it is possible to prevent an excessive overheating operation or a wet operation.
- the circulation amount according to the outside air temperature becomes natural as described above, The operation can be performed with the circulation amount according to the outside air temperature for each operation, and it is possible to prevent overheating operation and wet operation. Therefore, if the refrigerant adjustment container 30 is not provided in the refrigerant passage 24 or the like and is placed in another temperature environment that changes depending on the outside air temperature, the operation is performed with the circulation amount according to the outside air temperature. It is possible.
- the refrigerant in the refrigerant passage (refrigerant pipe) 24 and the refrigerant in the refrigerant adjustment container 30 are heated by attaching the refrigerant adjustment container 30 to the refrigerant passage 24.
- the refrigerant adjustment container 30 may be arranged along a pipe between the throttle 33 and the evaporator 18. That is, heat exchange between the refrigerant in the refrigerant adjustment container 30 and the refrigerant near the inlet of the evaporator 18 downstream of the throttle 33 is enabled.
- the refrigerant adjustment container 30 is provided with a heater H for adjusting the amount of the refrigerant.
- the refrigerant in the refrigerant adjustment container 30 exchanges heat with the low-temperature refrigerant immediately after passing through the throttle 33, so that the heat exchange can be reliably performed.
- the refrigerant adjustment container 30 is provided with a heater H for adjusting the amount of refrigerant, the heater H can adjust the temperature of the refrigerant adjustment container 30.
- the refrigeration cycle can be reliably operated with the refrigerant circulation amount corresponding to each season. That is, in this case, a temperature environment that changes depending on the outside air temperature is formed by heat exchange with the low-temperature refrigerant and heating of the heater H.
- the refrigerant adjustment container 30 is simply arranged at a position exposed to the outside air (for example, outside the casing in which the frozen cycle is stored). In this case, if the refrigerant adjustment container 30 is exposed to the outside air, the refrigerant adjustment container 30 is heated or cooled according to the temperature of the outside air. Further, since the evaporator 18 is provided with a fan 4 °, the refrigerant adjusting container 30 is arranged in an air passage formed by the fan 40. In this case, either upstream of the evaporator 18 or downstream of the evaporator 18. Also in this case, the temperature in the air passage depends on the outside air.
- the refrigerant regulating container 30 on the leeward side downstream of the evaporator 18.
- a Peltier element or the like may be used.
- the ⁇ ⁇ / che element means that when current flows through the contacts of different types of conductors (or semiconductors), This element can exhibit the Peltier effect, which is a phenomenon that generates or absorbs heat in addition to the heat generated. Therefore, in this case, the outside air temperature is detected (detected) by the outside air temperature thermistor 38, and the Peltier element is caused to generate heat * by the refrigerant adjustment container 30 based on the outside air temperature.
- the refrigerant adjustment container 30 may be configured to exchange heat with water.
- the cooling water can be composed of city water (tap water), water flowing out from the intake port 7 of the hot water storage tank 3 to the circulation path 9, and the like. Water
- the present invention is not limited to the above embodiments, and can be implemented with various modifications within the scope of the present invention.
- the refrigerant regulating container 30 when the refrigerant regulating container 30 is disposed in the refrigerant conduit 24 extending from the evaporator outlet to the compressor inlet, the refrigerant regulating container 30 is disposed closer to the evaporator 18 than the second passage 29 of the liquid-gas heat exchanger 27. It is also possible. Further, it may be either a structure without the throttle 33 or a structure without the liquid-gas heat exchanger 27.
- This refrigeration cycle can be used in various refrigeration systems such as air conditioners and showcases other than heat pump water heaters.
- refrigerants include ethylene.
- It may be a refrigerant used in supercritical conditions such as petane or nitric oxide.
- refrigerant used in supercritical conditions such as petane or nitric oxide.
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- General Engineering & Computer Science (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
Description
明 細 書 冷凍サイクル 技術分野 Description Refrigeration cycle technical field
この発明は、 冷凍サイクルに関し、 例えばヒートポンプ式給湯機の熱源ュニッ トに使用することができる冷凍サイクルに関するものである。 背景技術 The present invention relates to a refrigeration cycle, for example, a refrigeration cycle that can be used for a heat source unit of a heat pump water heater. Background art
ヒートポンプ式給湯機としては、 一般には図 6に示すように、 貯湯タンク 5 0 を有するタンクュニット 5 1と、 冷凍サイクル 5 2を有する熱源ュニット 5 3と を備える。 また、 冷凍サイクル 5 2は、 圧縮機 5 4と、 水熱交換器 (凝縮器) 5 5と、 膨張弁 5 7と、 蒸発器 5 8とを順に接続して構成される。 そして、 タンク ユニット 5 1は、 上記貯湯タンク 5 0と循環路 5 9とを備え、 この循環路 5 9に は、 水循環用ポンプ 6 0と熱交換路 6 1とが介設されている。 この場合、 熱交換 路 6 1は水熱交換器 5 5にて構成される。 As shown in FIG. 6, the heat pump water heater generally includes a tank unit 51 having a hot water storage tank 50 and a heat source unit 53 having a refrigeration cycle 52. The refrigeration cycle 52 is configured by connecting a compressor 54, a water heat exchanger (condenser) 55, an expansion valve 57, and an evaporator 58 in this order. The tank unit 51 includes the hot water storage tank 50 and a circulation path 59, and a water circulation pump 60 and a heat exchange path 61 are interposed in the circulation path 59. In this case, the heat exchange path 61 is constituted by a water heat exchanger 55.
上記装置においては、 圧縮機 5 4を駆動させると共に、 ポンプ 6 0を駆動 (作 動) させると、 貯湯タンク 5 0の底部に設けた取水口から貯溜水 (温湯) が循環 路 5 9に流出し、 これが熱交換路 6 1を流通する。 そのときこの温湯は水熱交換 器 5 5によって加熱され (沸き上げられ) 、 湯入口から貯湯タンク 5 0の上部に 返流される。 これによつて、 貯湯タンク 5 0に高温の温湯を貯めるものである。 また、 従来においては、 上記冷凍サイクルの冷媒として、 ジクロロジフルォロ メタン (R— 1 2 ) ゃクロロジフルォロメタン (R— 2 2 ) のような冷媒が使用 されてきたが、 オゾン層の破壊、 環境汚染等の問題から、 1 , 1 , 1 , 2—テト ラフルォロェタン (R— 1 3 4 a ) のような代替冷媒が使用されるようになって いる。 しかしながらこの R _ 1 3 4 aにおいても、 依然として地球温暖化能が高 いなどの問題があることから、 近年では、 このような問題のない自然系冷媒を使 用することが推奨されつつある。 この自然系冷媒として炭酸ガス等の超臨界冷媒 が有用であることは、 公知である。 ところが上記装置においては、 外気温度が変化することによって、 水熱交換器 (ガス冷却器) 側及び蒸発器側の負荷変動が生じ、 季節ごとに冷媒循環量が相違 する。 すなわち、 図 3に示すように、 外気温度が高い時 (高外気時) は Iのよう なサイクルとなり、 外気温度が低い時 (低外気時) は Πのようなサイクルとなり、 夏場 (高外気時) においては、 蒸発器 5 8内の冷媒密度が冬場 (低外気時) より も大となる。 このため、 季節ごとに最適な冷媒量での運転が困難であり、 夏場に おいては循環量が不足気味となって、 過度の過熱運転となり、 冬場においては循 環量が過剰気味となって湿り運転となり、 圧縮機の信頼性の低下を招くおそれが あった。 In the above device, when the compressor 54 is driven and the pump 60 is driven (operated), the stored water (hot water) flows out from the intake port provided at the bottom of the hot water storage tank 50 into the circulation path 59. This flows through the heat exchange path 61. At this time, the hot water is heated (boiled) by the water heat exchanger 55 and returned to the upper portion of the hot water storage tank 50 from the hot water inlet. With this, high-temperature hot water is stored in the hot water storage tank 50. Conventionally, refrigerants such as dichlorodifluoromethane (R-12) and chlorodifluoromethane (R-22) have been used as refrigerants in the refrigeration cycle. However, due to problems such as environmental pollution, alternative refrigerants such as 1,1,1,1,2-tetrahydrofluoretane (R-134a) have been used. However, R_134a still has problems such as high global warming ability. In recent years, it has been recommended to use natural refrigerants that do not have such problems. It is known that a supercritical refrigerant such as carbon dioxide is useful as the natural refrigerant. However, in the above-described apparatus, changes in the outside air temperature cause load fluctuations on the water heat exchanger (gas cooler) side and the evaporator side, and the amount of circulated refrigerant differs every season. That is, as shown in Fig. 3, when the outside air temperature is high (high outside air), the cycle is like I, and when the outside air temperature is low (low outside air), the cycle is like 、. In), the density of the refrigerant in the evaporator 58 becomes larger than in winter (at low outside air). For this reason, it is difficult to operate with the optimal refrigerant amount for each season, and in summer, the circulation amount tends to be insufficient, resulting in excessive overheating, and in winter, the circulation amount tends to be excessive. The operation was wet, which may have reduced the reliability of the compressor.
このため、 図 5に示すように、 高圧側に冷媒調整容器 6 5を設け、 流量調整弁 For this reason, as shown in FIG. 5, a refrigerant regulating container 65 is provided on the high pressure side, and a flow regulating valve is provided.
6 6を調整することによって、 この冷媒調整容器 (レシーバ) 6 5内の冷媒量を 増減させて、 外気温度に応じた冷媒循環量とすることも考えられる。 この場合、 高圧側において、 分岐すると共に、 この分岐部よりも下流側の位置において合流 するバイパス回路 6 7を設けると共に、 このバイパス回路 6 7に上記レシーバ 6 5を介設し、 さらに、 このレシーバ 6 5の出口側に流量調整弁 6 6を設ける。 す なわち、 バイパス回路 6 7は、 水熱交換器 5 5の上流側から分岐してレシーバ 6 5に接続される第 1通路 6 8と、 このレシーバ 6 5から導出されて第 1通路 6 8 の分岐部よりも下流側においてガス冷却器 5 5に合流する第 2通路 6 9とを備え、 第 2通路 6 9に上記調整弁 6 6が介設される。 また、 膨張弁 5 7と蒸発器 5 8と を接続する冷媒通路 7 0がこのレシーバ 6 5内を通過する。 By adjusting 66, the amount of refrigerant in the refrigerant adjustment container (receiver) 65 may be increased or decreased to obtain a refrigerant circulation amount according to the outside air temperature. In this case, on the high-pressure side, a bypass circuit 67 is provided which branches off at a position downstream of the branch portion, and the receiver 65 is provided in the bypass circuit 67. A flow control valve 66 is provided at the outlet side of 65. That is, the bypass circuit 67 includes a first passage 68 branched from the upstream side of the water heat exchanger 55 and connected to the receiver 65, and a first passage 68 derived from the receiver 65. And a second passage 69 that joins the gas cooler 55 at a downstream side of the branching part of the second passage. The above-mentioned regulating valve 66 is interposed in the second passage 69. Further, a refrigerant passage 70 connecting the expansion valve 57 and the evaporator 58 passes through the inside of the receiver 65.
従って、 図 5に示す冷凍サイクルでは、 バイパス回路 6 7を介してこのレシ一 バ 6 5内に入った高圧冷媒と、 この冷媒通路 7 0を流れる低圧冷媒との熱交換が 行われる。 そして、 調整弁 6 6の開度を調整することによって、 レシーバ 6 5内 を通過する冷媒流量を調整して、 レシーバ 6 5内の冷媒温度を調整する。 すなわ ち、 流量調整弁 6 6の開度制御によって、 要求された冷媒温度に保持し、 レシ一 バ 6 5內を適切な冷媒収容量とすることができ、 この回路内の冷媒循環量を最適 な量とすることができる。 Therefore, in the refrigeration cycle shown in FIG. 5, heat exchange is performed between the high-pressure refrigerant flowing into the receiver 65 via the bypass circuit 67 and the low-pressure refrigerant flowing through the refrigerant passage 70. Then, by adjusting the opening degree of the adjusting valve 66, the flow rate of the refrigerant passing through the receiver 65 is adjusted, and the temperature of the refrigerant in the receiver 65 is adjusted. In other words, by controlling the opening degree of the flow control valve 66, the required refrigerant temperature can be maintained, and the receiver 65 內 can have an appropriate refrigerant capacity, and the refrigerant circulation amount in this circuit can be reduced. The optimal amount can be used.
しかしながら、 図 5に示すような冷凍サイクルでは、 上記のように、 流量調整 弁 6 6を使用しなければならず、 コス ト高となる。 また、 高圧側においてガス冷 却器 5 5の途中にバイパス回路 6 7を設けるため、 回路構成が複雑化して製造し にくく、 コストが一層かかることになる。 しかも、 ガス冷却器 5 5を循環する冷 媒の一部をバイパスさせるため、 熱ロスとなり、 加熱能力を損なうおそれもある。 発明の開示 However, in a refrigeration cycle as shown in FIG. 5, as described above, the flow control valve 66 must be used, which increases the cost. Gas cooling on the high pressure side Since the bypass circuit 67 is provided in the middle of the cooler 55, the circuit configuration becomes complicated, it is difficult to manufacture, and the cost is further increased. In addition, since a part of the coolant circulating in the gas cooler 55 is bypassed, heat loss may occur and the heating capacity may be impaired. Disclosure of the invention
この発明は、 上記従来の欠点を解決するためになされたものであって、 その目 的は、 各季節に応じた冷媒循環量となって、 過熱運転や湿り運転を回避すること が可能であって、 しかも、 流量調整弁等を使用することなく、 低コストにて構成 することが可能な冷凍サイクルを提供することにある。 The present invention has been made in order to solve the above-mentioned conventional drawbacks. The purpose of the present invention is to provide a refrigerant circulation amount according to each season, thereby avoiding overheating operation and wet operation. Another object of the present invention is to provide a refrigeration cycle that can be configured at low cost without using a flow control valve or the like.
そこで、 この発明の冷凍サイクルは、 圧縮機からの吐出冷媒を、 ガス冷却器、 減圧機構、 蒸発器を順次経由させて上記圧縮機へと返流させる冷凍サイクルであ つて、 上記減圧機構と蒸発器との間の冷媒通路と冷媒調整容器とを、 接続通路を 介して接続し、 外気温度に依存して変化する温度環境下に上記冷媒調整容器を配 置したことを特徴としている。 Therefore, a refrigeration cycle of the present invention is a refrigeration cycle in which refrigerant discharged from a compressor is returned to the compressor through a gas cooler, a decompression mechanism, and an evaporator in order. The refrigerant adjustment container is connected to a refrigerant passage between the container and the refrigerant via a connection passage, and the refrigerant adjustment container is arranged in a temperature environment that changes depending on the outside air temperature.
この冷凍サイクルでは、 減圧機構と蒸発器との間の冷媒通路と冷媒調整容器と を、 接続通路を介して接続しているので、 冷媒調整容器内へは、 減圧機構と蒸発 器との間から冷媒 (ガス冷媒) が導入される。 そして、 この冷媒調整容器は外気 温度に依存して変化する温度環境下に置かれる。 そのため、 例えば、 夏場におい ては外気が高温であるので、 冷媒調整容器は高温側に保持され、 冷媒調整容器内 の貯留される冷媒量が少なくなり、 冷凍サイクルの循環路内の冷媒循環量を增加 させることができる。 また、 冬場においては外気が低温であるので、 冷媒調整容 器が低温側に保持され、 冷媒調整容器内に貯留される冷媒量が増加し、 冷凍サイ クルの循環路内の冷媒循環量を减少させることができる。 すなわち、 外気温度に 依存して変化する温度環境下に冷媒調整容器を置くことにより、 冷媒調整容器内 に貯留される冷媒量を増減させて、 外気温度に応じた冷媒循環量とすることがで さる。 In this refrigeration cycle, the refrigerant passage between the decompression mechanism and the evaporator and the refrigerant adjustment container are connected via the connection passage, so that the inside of the refrigerant adjustment container is provided between the decompression mechanism and the evaporator. Refrigerant (gas refrigerant) is introduced. The refrigerant adjustment container is placed in a temperature environment that changes depending on the outside air temperature. Therefore, for example, since the outside air is hot in summer, the refrigerant adjustment container is kept at a high temperature side, the amount of refrigerant stored in the refrigerant adjustment container decreases, and the refrigerant circulation amount in the circulation path of the refrigeration cycle decreases. Can be added. In addition, since the outside air is cold in winter, the refrigerant adjustment container is kept at a low temperature, the amount of refrigerant stored in the refrigerant adjustment container increases, and the amount of refrigerant circulating in the circulation path of the refrigeration cycle is reduced. Can be done. That is, by placing the refrigerant adjustment container in a temperature environment that changes depending on the outside air temperature, the amount of refrigerant stored in the refrigerant adjustment container can be increased or decreased to achieve a refrigerant circulation amount according to the outside air temperature. Monkey
このため、 各季節に応じた冷媒量でもって循環させることができ、 過度の過熱 運転や湿り運転となることを防止することができる。 しかも、 この冷媒循環量は、 調整弁が介設されるバイパス回路等を設けることなく、 外気温度に依存して変化 する温度環境によって調整することができる。 For this reason, the refrigerant can be circulated with the amount of refrigerant corresponding to each season, and it is possible to prevent an excessive overheating operation or a wet operation. Moreover, the amount of circulating refrigerant varies depending on the outside air temperature without providing a bypass circuit or the like in which a regulating valve is interposed. Can be adjusted according to the temperature environment.
一実施形態の冷凍サイクルは、 上記外気温度に依存して変化する温度環境を、 上記蒸発器出口から圧縮機吸入口に至る範囲の冷媒にて形成することを特徴とし ている。 The refrigeration cycle of one embodiment is characterized in that the temperature environment that changes depending on the outside air temperature is formed by a refrigerant ranging from the evaporator outlet to the compressor inlet.
上記実施形態の冷凍サイクルでは、 蒸発器出口から圧縮機吸入口に至る範囲の 冷媒は、 外気温度に応じて変化する。 このため、 この冷媒によって、 外気温度に 依存して変化する温度環境を安定して形成することができ、 確実に外気温度に応 じた冷媒循環量とすることができる。 In the refrigeration cycle of the above embodiment, the refrigerant ranging from the evaporator outlet to the compressor inlet changes according to the outside air temperature. Therefore, a temperature environment that changes depending on the outside air temperature can be stably formed by the refrigerant, and the amount of the circulated refrigerant corresponding to the outside air temperature can be ensured.
一実施形態の冷凍サイクルは、 上記冷媒調整容器が、 上記蒸発器出口から圧縮 機吸入口に至る冷媒配管に付設されて、 この冷媒配管内の冷媒と、 上記冷媒調整 容器内の冷媒とが熱交換されることを特徴としている。 In one embodiment, the refrigerant adjustment container is attached to a refrigerant pipe extending from the evaporator outlet to the compressor suction port, and the refrigerant in the refrigerant pipe and the refrigerant in the refrigerant adjustment container are heated. It is characterized by being exchanged.
上記実施形態の冷凍サイクルでは、 冷媒調整容器が、 蒸発器出口から圧縮機吸 入口に至る冷媒配管に付設されるので、 冷媒配管内の冷媒と、 冷媒調整容器内の 冷媒との熱交換の信頼性は高く、 安定して外気温度に応じた冷媒循環量とするこ とができる。 In the refrigeration cycle of the above embodiment, since the refrigerant adjustment container is attached to the refrigerant pipe extending from the evaporator outlet to the compressor intake, the reliability of heat exchange between the refrigerant in the refrigerant pipe and the refrigerant in the refrigerant adjustment container is reduced. The refrigerant circulation rate is high, and the refrigerant circulation amount can be stably set according to the outside air temperature.
一実施形態の冷凍サイクルは、 上記減圧機構と蒸発器との間の冷媒通路におい て、 上記接続通路の接続部よりも上記蒸発器側に絞りを介設したことを特徴とし ている。 The refrigeration cycle of one embodiment is characterized in that, in a refrigerant passage between the decompression mechanism and the evaporator, a throttle is provided on the evaporator side from a connection portion of the connection passage.
上記実施形態の冷凍サイクルでは、 絞りを設けることにより、 最適な吸入過熱 度をつけることができる。 In the refrigeration cycle of the above embodiment, by providing the throttle, an optimal suction superheat degree can be provided.
一実施形態の冷凍サイクルは、 上記冷媒調整容器を、 外気にさらすように配置 したことを特徴としている。 The refrigeration cycle of one embodiment is characterized in that the refrigerant adjustment container is arranged so as to be exposed to the outside air.
上記実施形態の冷凍サイクルでは、 冷媒調整容器が外気にさらされるので、 冷 媒調整容器内の冷媒がその外気によって暖められたり、 冷やされたりする。 すな わち、 簡単な構成にて、 外気温度に応じてこの冷媒調整容器内の冷媒が増減して、 各季節に応じた冷媒循環量となる。 In the refrigeration cycle of the above embodiment, since the refrigerant adjustment container is exposed to the outside air, the refrigerant in the refrigerant adjustment container is warmed or cooled by the outside air. In other words, with a simple configuration, the amount of refrigerant in the refrigerant adjustment container increases and decreases according to the outside air temperature, and the amount of refrigerant circulated according to each season.
一実施形態の冷凍サイクルは、 上記冷媒調整容器を、 上記蒸発器に付設される ファンにて生じる風通路内に配置したことを特徴としている。 The refrigeration cycle of one embodiment is characterized in that the refrigerant adjustment container is arranged in an air passage formed by a fan attached to the evaporator.
上記実施形態の冷凍サイクルでは、 冷媒調整容器を蒸発器に付設されるファン にて生じる風通路内に配置したので、 この風によつて冷媒調整容器の温度を調整 することができる。 In the refrigeration cycle of the above embodiment, the refrigerant adjustment container is provided with a fan attached to the evaporator. The temperature of the refrigerant adjustment container can be adjusted by this wind, since it is arranged in the wind passage generated by the above.
一実施形態の冷凍サイクルは、 上記冷媒調整容器を、 上記蒸発器よりも下流の 風下側に配置したことを特徴としている。 In one embodiment, the refrigeration cycle is characterized in that the refrigerant adjustment container is arranged on the leeward side downstream of the evaporator.
上記実施形態の冷凍サイクルでは、 冷媒調整容器を蒸発器よりも下流の風下側 に配置したので、 熱交換上好ましいものとなって、 冷媒調整容器の温度の調整を 確実に行うことがきる。 In the refrigeration cycle of the above embodiment, the refrigerant adjustment container is arranged downstream of the evaporator on the leeward side, which is preferable in terms of heat exchange, and the temperature of the refrigerant adjustment container can be surely adjusted.
一実施形態の冷凍サイクルは、 上記外気温度に依存して変化する温度環境を、 ペルチェ素子等にて上記冷媒調整容器を加熱又は冷却することにより構成するこ とを特徴としている。 The refrigeration cycle of one embodiment is characterized in that the temperature environment that changes depending on the outside air temperature is configured by heating or cooling the refrigerant adjustment container with a Peltier element or the like.
上記実施形態の冷凍サイクルでは、 冷媒調整容器を、 ペルチェ素子等にて加熱 又は冷却することができるので、 冷媒調整容器内の冷媒の外気温度に応じた増減 を確実に行わせることができ、 各季節に応じたものに安定して冷媒循環量を調整 できる。 In the refrigeration cycle of the above embodiment, the refrigerant adjustment container can be heated or cooled by a Peltier element or the like, so that the refrigerant in the refrigerant adjustment container can be reliably increased or decreased according to the outside air temperature. The refrigerant circulation amount can be adjusted stably according to the season.
一実施形態の冷凍サイクルは、 上記冷媒調整容器を、 外気温度に依存して温度 変化する水と熱交換するように配置したことを特徴としている。 The refrigeration cycle of one embodiment is characterized in that the refrigerant adjustment container is arranged to exchange heat with water whose temperature changes depending on the outside air temperature.
上記実施形態の冷凍サイクルでは、 冷媒調整容器が、 その温度が外気に依存す る水によって温度調整される。 すなわち、 外気温度に応じてこの冷媒調整容器内 の冷媒が増減して、 各季節に応じた冷媒循環量となる。 In the refrigeration cycle of the above embodiment, the temperature of the refrigerant adjustment container is adjusted by water whose temperature depends on the outside air. That is, the amount of refrigerant in the refrigerant adjustment container increases and decreases according to the outside air temperature, and the amount of refrigerant circulated according to each season.
一実施形態の冷凍サイクルは、 上記減圧機構と蒸発器との間の冷媒通路におい て、 上記接続通路の接続部よりも上記蒸発器側に絞りを介設し、 上記冷媒調整容 器内の冷媒と、 上記絞りよりも下流側の蒸発器の入口近傍の冷媒とを熱交換させ、 さらに、 冷媒調整容器には冷媒量調整用のヒータ Hを付設したことを特徴として いる。 In one embodiment, a refrigeration cycle includes a refrigerant passage between the decompression mechanism and the evaporator, wherein a throttle is provided on the evaporator side of a connection portion of the connection passage, and a refrigerant in the refrigerant adjustment container is provided. And heat exchange between the refrigerant and the refrigerant in the vicinity of the inlet of the evaporator on the downstream side of the throttle. Further, the refrigerant adjustment container is provided with a heater H for adjusting the amount of refrigerant.
上記実施形態の冷凍サイクルでは、 冷媒調整容器内の冷媒は、 絞りを通過した 直後の低温冷媒と熱交換されるので、 熱交換を確実に行わせることができ、 しか も、 冷媒調整容器には冷媒量調整用のヒータを付設したので、 ヒータにて外気温 度に応じて冷媒調整容器の温度調整することができる。 In the refrigeration cycle of the above embodiment, the refrigerant in the refrigerant adjustment container exchanges heat with the low-temperature refrigerant immediately after passing through the throttle, so that the heat exchange can be reliably performed. Since a heater for adjusting the amount of refrigerant is provided, the temperature of the refrigerant adjustment container can be adjusted according to the outside air temperature by the heater.
一実施形態の冷凍サイクルは、 高圧側が超臨界圧力で運転することを特徴とし ている。 The refrigeration cycle of one embodiment is characterized in that the high pressure side operates at supercritical pressure. ing.
上記実施形態の冷凍サイクルでは、 高圧側が超臨界圧力で運転するものである ので、 冷媒に超臨界で使用する超臨界冷媒を用いることになり、 地球環境に優し い冷凍サイクノレとなる。 また、 超臨界冷媒を用いた冷凍サイクルによれば、 高圧 側の圧力が高くなるので、 冷媒調整容器を低圧側に設けることによる利点を充分 に生かすことができ、 上記実施形態の作用を特に有効に発揮することができる。 図面の簡単な説明 In the refrigeration cycle of the above embodiment, since the high pressure side operates at a supercritical pressure, a supercritical refrigerant used in a supercritical state is used as a refrigerant, and a refrigeration cycle that is friendly to the global environment. Further, according to the refrigeration cycle using a supercritical refrigerant, the pressure on the high pressure side increases, so that the advantage of providing the refrigerant adjustment container on the low pressure side can be fully utilized, and the operation of the above embodiment is particularly effective. Can be demonstrated. BRIEF DESCRIPTION OF THE FIGURES
図 1は、 この兖明の冷凍サイクルの実施形態を示す簡略図である。 FIG. 1 is a simplified diagram showing an embodiment of the refrigeration cycle of the present invention.
図 2は、 上記冷凍サイクルのモリエル線図である。 FIG. 2 is a Mollier diagram of the refrigeration cycle.
図 3は、 従来の冷凍サイクルのモリエノレ線図である。 FIG. 3 is a Mollier diagram of a conventional refrigeration cycle.
図 4は、 この発明の冷凍サイクルの他の実施形態を示す要部簡略図である。 図 5は、 冷凍サイクルの比較例を示す簡略図である。 FIG. 4 is a simplified view of a main part showing another embodiment of the refrigeration cycle of the present invention. FIG. 5 is a simplified diagram showing a comparative example of a refrigeration cycle.
図 6は、 従来の冷凍サイクルの簡略図である。 発明を実施するための最良の形態 FIG. 6 is a simplified diagram of a conventional refrigeration cycle. BEST MODE FOR CARRYING OUT THE INVENTION
この発明の冷凍サイクルの具体的な実施の形態について、 図面を参照しつつ詳 細に説明する。 図 1はこの冷凍サイクルを使用したヒートポンプ式給湯機の簡略 図を示し、 このヒートポンプ式給湯機は、 タンクユニット 1と熱源ユニット 2を 備え、 タンクュニット 1の水 (温湯) を熱源ュニット 2にて加熱するものである。 タンクユニット 1は貯湯タンク 3を備え、 この貯湯タンク 3に貯湯された温湯 が図示省略の浴槽等に供給される。 すなわち、 貯湯タンク 3には、 その底壁に給 水口 5が設けられると共に、 その上壁に出湯口 6が設けられている。 そして、 給 水口 5から貯湯タンク 3に市水 (水道水) が供給され、 出湯口 6から高温の温湯 が出湯される。 また、 貯湯タンク 3には、 その底壁に取水口 7が開設されると共 に、 側壁 (周壁) の上部に湯入口 8が開設され、 取水口 7と湯入口 8とが循環路 9にて連結されている。 そして、 この循環路 9に水循環用ポンプ 1 0と熱交換路 1 1とが介設されている。 Specific embodiments of the refrigeration cycle of the present invention will be described in detail with reference to the drawings. Figure 1 shows a simplified diagram of a heat pump water heater using this refrigeration cycle. This heat pump water heater has a tank unit 1 and a heat source unit 2, and heats water (hot water) in tank unit 1 with heat source unit 2. Is what you do. The tank unit 1 has a hot water storage tank 3, and the hot water stored in the hot water storage tank 3 is supplied to a bathtub or the like (not shown). That is, the hot water storage tank 3 is provided with a water supply port 5 on a bottom wall thereof and a tap hole 6 on an upper wall thereof. Then, city water (tap water) is supplied from the water supply port 5 to the hot water storage tank 3, and high-temperature hot water is supplied from the water supply port 6. In addition, the hot water storage tank 3 has a water inlet 7 at the bottom wall and a hot water inlet 8 at the top of the side wall (peripheral wall), and the water inlet 7 and the hot water inlet 8 pass through the circulation path 9. Connected. The circulation path 9 is provided with a water circulation pump 10 and a heat exchange path 11.
次に、 熱源ユニット 2はこの実施の形態に係る冷凍サイクル Rを備え、 この冷 凍サイクル Rは、 圧縮機 1 5と、 熱交換路 1 1を構成する水熱交換器 (ガス冷却 器) 1 6と、 減圧機構 (電動膨張弁) 1 7と、 空気熱交換器 (蒸発器) 1 8とを 順に接続して構成される。 すなわち、 圧縮機 1 5の吐出口と、 ガス冷却器 1 6と を冷媒通路 2 0にて接続し、 ガス冷却器 1 6と電動膨張弁 1 Ίとを冷媒通路 2 1 にて接続し、 電動膨張弁 1 7と蒸発器 1 8とを冷媒通路 2 2にて接続し、 蒸発器 1 8と圧縮機 1 5とをアキュームレータ 2 3が介設された冷媒通路 2 4にて接続 している。 そして、 冷媒としては、 例えば、 高圧側を超臨界圧力で使用する炭酸 ガス (C 0 2 ) を用いる。 なお、 水熱交換器 1 6としてのガス冷却器は、 圧縮機 1 5にて圧縮された高温 ·高圧の超臨界冷媒を冷却する機能を有するものである。 また、 上記冷媒通路 2 0には、 圧力保護スィッチとしての H P S 2 5と、 圧力 センサ 2 6とが設けられている。 さらに、 上記蒸発器 1 8には、 能力調整用のフ アン 4 0が付設されている。 Next, the heat source unit 2 includes the refrigeration cycle R according to this embodiment. The freezing cycle R consists of a compressor 15, a water heat exchanger (gas cooler) 16, which constitutes the heat exchange path 11, a pressure reducing mechanism (electric expansion valve) 17, and an air heat exchanger (evaporator). 1) and 8 are connected in order. That is, the discharge port of the compressor 15 and the gas cooler 16 are connected through the refrigerant passage 20, the gas cooler 16 and the electric expansion valve 1 are connected through the refrigerant passage 21, The expansion valve 17 and the evaporator 18 are connected by a refrigerant passage 22, and the evaporator 18 and the compressor 15 are connected by a refrigerant passage 24 provided with an accumulator 23. As the refrigerant, for example, carbon dioxide gas (C 0 2 ) whose high pressure side is used at a supercritical pressure is used. The gas cooler as the water heat exchanger 16 has a function of cooling the high-temperature and high-pressure supercritical refrigerant compressed by the compressor 15. The refrigerant passage 20 is provided with an HPS 25 as a pressure protection switch and a pressure sensor 26. Further, the evaporator 18 is provided with a fan 40 for adjusting the capacity.
また、 この冷凍サイクル Rには、 ガス冷却器 1 6から流出した高圧冷媒を冷却 する液ガス熱交換器 2 7を備える。 この場合、 この液ガス熱交換器 2 7は、 例え ば、 二重管構造であって、 ガス冷却器 1 6からの冷媒が通過する第 1通路 2 8と、 蒸発器 1 8からの冷媒が通過する第 2通路 2 9とを備える。 すなわち、 第 1通路 2 8力 ガス冷却器 1 6と電動膨張弁 1 7とを連結する冷媒通路 2 1の一部を構 成し、 第 2通路 2 9が、 蒸発器 1 8と圧縮機 1 5とを連結する冷媒通路 2 4の一 部を構成する。 このため、 第 1通路 2 8を通過する高圧高温の冷媒と第 2通路 2 9を通過する低圧低温の冷媒との間で熱交換され、 ガス冷却器 1 6からの冷媒に 過冷却を付与し、 また、 アキュームレータ 2 3に入る冷媒を加熱して、 圧縮機 1 5の湿り圧縮を防止することができる。 Further, the refrigeration cycle R includes a liquid-gas heat exchanger 27 for cooling the high-pressure refrigerant flowing out of the gas cooler 16. In this case, the liquid-gas heat exchanger 27 has, for example, a double-pipe structure, in which a first passage 28 through which the refrigerant from the gas cooler 16 passes, and a refrigerant from the evaporator 18. A second passage 29 passing therethrough. That is, the first passage 28 constitutes a part of the refrigerant passage 21 connecting the gas cooler 16 and the electric expansion valve 17, and the second passage 29 constitutes the evaporator 18 and the compressor 1. A part of the refrigerant passage 24 that connects to the refrigerant passage 5 is formed. Therefore, heat is exchanged between the high-pressure and high-temperature refrigerant passing through the first passage 28 and the low-pressure and low-temperature refrigerant passing through the second passage 29, and supercools the refrigerant from the gas cooler 16. Also, the refrigerant entering the accumulator 23 can be heated to prevent wet compression of the compressor 15.
さらに、 この冷凍サイクル Rには、 冷媒調整容器 3 0が上記冷媒通路 2 4 (蒸 発器出口から圧縮機吸入口に至る冷媒配管であって、 さらに具体的には、 液ガス 熱交換器 2 7の第 2通路 2 9とアキュームレータ 2 3との間) に付設されている。 このため、 冷媒調整容器 3 0は冷媒通路 2 4と接触し、 この冷媒調整容器 3 0内 の冷媒と冷媒通路 2 4内の冷媒との熱交換が可能とされている。 また、 この冷媒 調整容器 3 0には接続通路 3 1が接続される。 すなわち、 この接続通路 3 ].は、 上記冷媒通路 2 2 (減圧機構 1 7と蒸発器 1 8との間の冷媒通路) と、 冷媒調整 容器 3 0とを接続するものである。 このため、 この冷凍サイクル Rの冷媒 (ガス 冷媒) が減圧機構 1 7と蒸発器 1 8との間から引き出されて、 冷媒調整容器 3 0 に液冷媒として貯留する。 なお、 この冷媒調整容器 3 0の容量としては、 このサ ィクル (圧縮機 1 5→ガス冷却器 1 6→減圧機構 1 7→蒸発器 1 8→圧縮機 1 5 と冷媒が循環する循環路) の全容量の 1 / 1 0程度 (例えば、 3 0 0〜4 0 0 c c程度) とするのが好ましい。 Further, in the refrigeration cycle R, the refrigerant adjustment container 30 is a refrigerant pipe extending from the outlet of the evaporator to the inlet of the compressor, and more specifically, the liquid gas heat exchanger 2. 7 between the second passage 29 and the accumulator 23). Therefore, the refrigerant adjustment container 30 comes into contact with the refrigerant passage 24, and heat exchange between the refrigerant in the refrigerant adjustment container 30 and the refrigerant in the refrigerant passage 24 is enabled. Further, a connection passage 31 is connected to the refrigerant adjustment container 30. That is, the connection passage 3] is connected to the refrigerant passage 22 (a refrigerant passage between the pressure reducing mechanism 17 and the evaporator 18), It connects the container 30. Therefore, the refrigerant (gas refrigerant) of the refrigeration cycle R is drawn out from between the decompression mechanism 17 and the evaporator 18 and stored in the refrigerant adjustment container 30 as a liquid refrigerant. The capacity of the refrigerant adjustment container 30 is determined by the cycle (compressor 15 → gas cooler 16 → decompression mechanism 17 → evaporator 18 → compressor 15 → circulation path through which the refrigerant circulates) About 1/10 of the total capacity (for example, about 300 to 400 cc).
そして、 減圧機構 1 7と蒸発器 1 8との間の冷媒通路 2 2において、 接続通路 3 1の接続部 3 2 (A点) よりも蒸発器 1 8側に絞り 3 3を介設している。 なお、 この絞り 3 3としては、 キヤビラリ一チューブ等の固定絞りを使用することがで きる力 もちろん電動膨張弁等にても構成することができる。 また、 この絞り 3 3としては、 例えば、 外気温度が 7 °Cで、 この冷凍サイクルが 4 5 0 O Wの加熱 能力である場合に、 3〜5 °Cの吸入過熱度となる絞りを選択するのが好ましい。 ところで、 このヒートポンプ給湯機は、 循環路 9の熱交換路 1 1よりも上流側 の温度を検出する温度センサ (入水サーミスタ) 3 4と、 循環路 9の熱交換路 1 1よりも下流側の温度を検出する温度センサ (出湯サーミスタ) 3 5と、 蒸発器 1 8の温度を検出する温度センサ (空気熱交サーミスタ) 3 6、 圧縮機 1 5の吐 出温度を検出する温度センサ (吐出管サーミスタ) 3 7と、 外気温度を検出する 温度センサ (外気温度サーミスタ) 3 8等が設けられている。 そして、 これらの センサからのデータ (検出された温度) がこのヒートポンプ給湯機の図示省略の 制御部 (例えば、 マイクロコンピュータ等からなる) に入力され、 これらのデー タに基づいて、 各種の制御が行われる。 Then, in the refrigerant passage 22 between the pressure reducing mechanism 17 and the evaporator 18, a throttle 33 is provided on the evaporator 18 side from the connection portion 32 (point A) of the connection passage 31. I have. It should be noted that as the throttle 33, a force capable of using a fixed throttle such as a capillary tube or the like can be used as well as an electric expansion valve or the like. Further, as the throttle 33, for example, when the outside air temperature is 7 ° C and the refrigeration cycle has a heating capacity of 450 OW, a throttle having a suction superheat of 3 to 5 ° C is selected. Is preferred. By the way, this heat pump water heater has a temperature sensor (input water thermistor) 34 that detects the temperature of the circulation path 9 on the upstream side of the heat exchange path 11, and the temperature sensor on the downstream side of the heat exchange path 11 of the circulation path 9. Temperature sensor (outlet hot water thermistor) 35 that detects the temperature, temperature sensor (air heat exchange thermistor) 36 that detects the temperature of the evaporator 18, temperature sensor (the discharge pipe) that detects the discharge temperature of the compressor 15 Thermistor) 37 and a temperature sensor (outside air temperature thermistor) 38 that detects the outside air temperature are provided. Then, data (detected temperature) from these sensors is input to a control unit (not shown) (not shown) of the heat pump water heater, and various controls are performed based on the data. Done.
すなわち、 ヒートポンプ式給湯機の運転時には、 例えば、 吐出管サーミスタ 3 7にて吐出管の温度が検出され、 この吐出管温度を目標吐出管温度となるように、 電動膨張弁 1 7の開度を調整 (制御) することができる。 また、 入水サーミスタ 3 4の温度が所定温度 (例えば、 6 0 °C) 以上であれば、 貯湯タンク 3内の湯が 沸き上がつているとして運転を停止させたり、 また、 外気温度サーミスタ 3 8の 温度に基づいて、 圧縮機 1 5の運転周波数を制御して、 湯加熱能力 (沸上能力) 等を調整したりすることができる。 That is, during operation of the heat pump water heater, for example, the temperature of the discharge pipe is detected by the discharge pipe thermistor 37, and the opening of the electric expansion valve 17 is adjusted so that the discharge pipe temperature becomes the target discharge pipe temperature. It can be adjusted (controlled). If the temperature of the water input thermistor 34 is equal to or higher than a predetermined temperature (for example, 60 ° C.), it is determined that the hot water in the hot water storage tank 3 is boiling, and the operation is stopped. Based on the temperature, the operating frequency of the compressor 15 can be controlled to adjust the hot water heating capacity (boiling capacity) and the like.
次に、 このヒートポンプ式給湯機の運転動作 (湯沸かし運転) を説明する。 圧 縮機 1 5を駆動させると共に、 水循環用ポンプ 1 0を駆動 (作動) させる。 する と、 貯湯タンク 3の底部に設けた取水口 7から貯溜水 (温湯) が流出し、 これが 循環路 9の熱交換路 1 1を流通する。 また、 圧縮機 1 5からの吐出冷媒が、 ガス 冷却器 1 6、 減圧機構 1 7、 蒸発器 1 8とを順次経由して上記圧縮機 1 5へと返 流する。 そのため、 循環路 9の熱交換路 1 1を流通する水がガス冷却器 1 6であ る水熱交換器によって加熱され (沸き上げられ) 、 湯入口 8から貯湯タンク 3の 上部に返流される。 そしてこのような動作を継続して行うことによって、 貯湯タ ンク 3に温湯が貯湯されることになる。 なお、 現状の電力料金制度は夜間の電力 料金単価が昼間に比べて低く設定されているので、 この運転は、 低額である深夜 時間帯に行い、 コストの低減を図るようにするのが好ましい。 Next, the operation of the heat pump water heater (boiler operation) will be described. Pressure The compressor 15 is driven and the water circulation pump 10 is driven (operated). Then, the stored water (hot water) flows out of the water intake port 7 provided at the bottom of the hot water storage tank 3 and flows through the heat exchange path 11 of the circulation path 9. Further, the refrigerant discharged from the compressor 15 is returned to the compressor 15 via the gas cooler 16, the pressure reducing mechanism 17, and the evaporator 18 in order. Therefore, the water flowing through the heat exchange path 11 of the circulation path 9 is heated (boiled) by the water heat exchanger which is the gas cooler 16, and is returned from the hot water inlet 8 to the upper part of the hot water storage tank 3. You. Then, by continuing such an operation, hot water is stored in the hot water storage tank 3. In the current electricity tariff system, the unit price of electricity at night is set lower than that of daytime, so it is preferable to perform this operation during the late night hours when the cost is low to reduce costs.
この運転の際のモリエル線図は図 2のようになる。 すなわち、 この冷凍サイク ルにおいては、 1の状態の高圧冷媒が圧縮機 1 5から吐出され、 この高圧冷媒が ガス冷却器 1 6 (水熱交換器) に導入される。 このガス冷却器 1 6では、 熱交換 路 1 1を通過する水と熱交換を行う。 これによつて、 この熱交換路 1 1を通過す る水は加熱される (沸き上げられる) 。 そして、 この熱交換により、 高圧冷媒は 水に対して放熱し、 そのェンタルビが 1から 2の状態にまで低下する。 この 2の 状態の高圧冷媒が减圧機構 1 7 (膨張弁) に送られる。 この減圧機構 1 7でこの 高圧冷媒が A点まで減圧され、 さらに、 絞り 3 3で 3の状態まで低下する。 そし て、 この低圧冷媒が蒸発器 1 8へ導入される。 この蒸発器 1 8では、 この低圧冷 媒が空気と熱交換を行う。 この熱交換により、 低圧冷媒は吸熱して蒸発して、 B 点では④の状態となる。 すなわち、 そのェンタルビが 3から 4の状態まで増大し、 この 4の状態の低圧冷媒が圧縮機 1 5 へ送られる。 The Mollier diagram for this operation is shown in Figure 2. That is, in this refrigeration cycle, the high-pressure refrigerant in the state 1 is discharged from the compressor 15 and the high-pressure refrigerant is introduced into the gas cooler 16 (water heat exchanger). The gas cooler 16 exchanges heat with water passing through the heat exchange path 11. As a result, the water passing through the heat exchange path 11 is heated (boiled). Then, due to this heat exchange, the high-pressure refrigerant radiates heat to the water, and its enthalpy drops from 1 to 2. The high-pressure refrigerant in these two states is sent to the low-pressure mechanism 17 (expansion valve). The high-pressure refrigerant is depressurized to the point A by the pressure reducing mechanism 17, and further reduced to the state of 3 by the throttle 33. Then, the low-pressure refrigerant is introduced into the evaporator 18. In the evaporator 18, the low-pressure refrigerant exchanges heat with air. Due to this heat exchange, the low-pressure refrigerant absorbs heat and evaporates. That is, the enthalpy increases from 3 to 4, and the low-pressure refrigerant in this 4 state is sent to the compressor 15.
この場合、 減圧機構 1 7と蒸発器 1 8との間の冷媒通路 2 2における接続通路 3 1との接続部 3 2 (A点) での状態の冷媒が、 蒸発器出口から圧縮機吸入口に 至る配管であって、 液ガス熱交換器 2 7の第 2通路 2 9とアキュームレータ 2 3 との間 (B点) での冷媒と熱交換される。 このため、 上記 B点での温度が外気に 応じて上昇すれば、 冷媒調整容器 3 0の温度も上昇して、 冷媒貯留量が減少し、 また、 上記 B点での温度が外気に応じて下降すれば、 上記冷媒調整容器 3 0での 温度も下降して、 冷媒貯留量が増加する。 そして、 図 2の破線 m) で示す ように A点と B点とで温度差がなくなれば、 冷媒調整容器 3 0内の冷媒貯留量の 変化がなくなり、 一定の冷媒循環量でもって冷媒が循環することになる。 このよ うに、 この冷凍サイクル Rでは A点の温度と B点の温度とがほぼ等しくなる。 そ の一方、 絞り 3 3を設けているので、 図 2に示すように、 B点での温度が、 蒸発 温度にこの絞り 3 3の圧力降下に見合う温度が付加されたもの (A点での温度) となって、 圧力降下に見合う一定の過熱度 ( S ) を得ることができ、 効率の良い 運転が可能となっている。 In this case, the refrigerant at the connection point 32 (point A) of the refrigerant passage 22 between the pressure reducing mechanism 17 and the evaporator 18 and the connection passage 31 flows from the evaporator outlet to the compressor inlet. And heat is exchanged with the refrigerant between the second passage 29 of the liquid-gas heat exchanger 27 and the accumulator 23 (point B). For this reason, if the temperature at the point B rises in accordance with the outside air, the temperature of the refrigerant regulating container 30 also rises, and the refrigerant storage amount decreases, and the temperature at the point B rises in accordance with the outside air. If the temperature decreases, the temperature in the refrigerant adjustment container 30 also decreases, and the amount of stored refrigerant increases. And it is shown by the broken line m) in Fig. 2. As described above, when the temperature difference between the points A and B disappears, the refrigerant storage amount in the refrigerant adjustment container 30 does not change, and the refrigerant circulates with a constant refrigerant circulation amount. Thus, in the refrigeration cycle R, the temperature at the point A and the temperature at the point B are almost equal. On the other hand, since the throttle 33 is provided, as shown in Fig. 2, the temperature at point B is obtained by adding the temperature corresponding to the pressure drop of this throttle 33 to the evaporation temperature (at point A). Temperature), a constant superheat (S) commensurate with the pressure drop can be obtained, and efficient operation is possible.
ところで、 蒸発器出口から圧縮機吸入口に至る冷媒配管 (冷媒通路 2 4 ) は、 外気温度の影響を受け、 外気温度が高温である夏場においては、 外気温度が低温 である冬場よりも高温である。 そのため、 図 3に示すように、 外気温度が高い時 (高外気時) は Iのようなサイクルとなり、 外気温度が低い時 (低外気温時) は Πのようなサイクノレとなり、 夏場 (高外気温時) においては、 蒸発器 1 8内の密 度が冬場 (低外気温時) よりも大となる。 このため、 高外気温時と低外気温時と では蒸発器 1 8内の冷媒量差が大であり、 高外気温時に多くの冷媒循環量が必要 であるにもかかわらず、 この冷媒循環量を確保することができず、 また、 低外気 温時では少ない冷媒循環量でよいのにもかかわらず、 冷媒循環量が多くなってい た。 By the way, the refrigerant pipe (refrigerant passage 24) from the evaporator outlet to the compressor inlet is affected by the outside air temperature, and in summer when the outside air temperature is high, it is higher than in winter when the outside air temperature is low. is there. Therefore, as shown in Fig. 3, when the outside air temperature is high (high outside air), a cycle like I occurs, and when the outside air temperature is low (low outside air temperature), a cycle like と な り occurs. At the time of temperature), the density inside the evaporator 18 is higher than in winter (at low outside temperature). Therefore, there is a large difference in the amount of refrigerant in the evaporator 18 between the high outside temperature and the low outside temperature. And the amount of circulating refrigerant was large at low outside air temperatures, despite the small amount of circulating refrigerant.
しかしながら、 冷媒調整容器 3 0と接続通路 3 1とを設けることによって、 夏 場においては外気が高温であるので、 冷媒調整容器 3 0は高温側に保持され、 冷 媒調整容器 3 0内の貯留される冷媒量が少なくなり、 冷凍サイクルの循環路内の 冷媒循環量を増加させることができる。 また、 冬場においては外気が低温である ので、 冷媒調整容器 3 0が低温側に保持され、 冷媒調整容器 3 0内に貯留される 冷媒量が増加し、 冷凍サイクルの循環路内の冷媒循環量を減少させることができ る。 すなわち、 外気温度に依存して変化する温度環境下に冷媒調整容器 3 0を置 くことにより、 冷媒調整容器 3 0内の冷媒量を増減させて、 外気温度に応じた冷 媒循環量とすることができる。 このため、 各季節に応じた冷媒量でもって循環さ せることができ、 過度の過熱運転や湿り運転となることを防止することができる。 ところで、 冷媒調整容器 3 0を外気温度に依存して変化する温度環境下に配置 することによって、 上記のように、 外気温度に応じた循環量に自然となり、 季節 毎の外気温度に応じた循環量で運転することができ、 過熱運転や湿り運転となる のを防止することができる。 従って、 冷媒調整容器 3 0を、 冷媒通路 2 4等に付 設させることなく、 外気温度に依存して変化する他の温度環境下に置ければ、 外 気温度に応じた循環量で運転することが可能である。 However, by providing the refrigerant adjustment container 30 and the connection passage 31, since the outside air has a high temperature in summer, the refrigerant adjustment container 30 is kept on the high temperature side and stored in the refrigerant adjustment container 30. As a result, the amount of refrigerant to be cooled is reduced, and the amount of refrigerant circulated in the circulation path of the refrigeration cycle can be increased. In winter, since the outside air is at a low temperature, the refrigerant adjustment container 30 is kept at a low temperature, the amount of refrigerant stored in the refrigerant adjustment container 30 increases, and the refrigerant circulation amount in the circulation path of the refrigeration cycle. Can be reduced. That is, by placing the refrigerant adjustment container 30 in a temperature environment that changes depending on the outside air temperature, the amount of refrigerant in the refrigerant adjustment container 30 is increased or decreased to obtain a refrigerant circulation amount according to the outside air temperature. be able to. For this reason, it is possible to circulate the refrigerant with the amount of refrigerant according to each season, and it is possible to prevent an excessive overheating operation or a wet operation. By arranging the refrigerant adjustment container 30 in a temperature environment that changes depending on the outside air temperature, the circulation amount according to the outside air temperature becomes natural as described above, The operation can be performed with the circulation amount according to the outside air temperature for each operation, and it is possible to prevent overheating operation and wet operation. Therefore, if the refrigerant adjustment container 30 is not provided in the refrigerant passage 24 or the like and is placed in another temperature environment that changes depending on the outside air temperature, the operation is performed with the circulation amount according to the outside air temperature. It is possible.
また、 上記実施の形態では、 冷媒調整容器 3 0を冷媒通路 2 4に付設すること によって、 この冷媒通路 (冷媒配管) 2 4内の冷媒と、 冷媒調整容器 3 0内の冷 媒とを熱交換させるものであるが、 図 4に示すように、 冷媒調整容器 3 0を絞り 3 3と蒸発器 1 8の間の配管に沿わせてもよい。 すなわち、 冷媒調整容器 3 0内 の冷媒と、 絞り 3 3よりも下流側の蒸発器 1 8の入口近傍の冷媒との熱交換を可 能としている。 この場合、 冷媒調整容器 3 0には冷媒量調整用のヒータ Hを付設 している。 Further, in the above-described embodiment, the refrigerant in the refrigerant passage (refrigerant pipe) 24 and the refrigerant in the refrigerant adjustment container 30 are heated by attaching the refrigerant adjustment container 30 to the refrigerant passage 24. Although it is exchanged, as shown in FIG. 4, the refrigerant adjustment container 30 may be arranged along a pipe between the throttle 33 and the evaporator 18. That is, heat exchange between the refrigerant in the refrigerant adjustment container 30 and the refrigerant near the inlet of the evaporator 18 downstream of the throttle 33 is enabled. In this case, the refrigerant adjustment container 30 is provided with a heater H for adjusting the amount of the refrigerant.
この図 4のように構成すれば、 冷媒調整容器 3 0内の冷媒は、 絞り 3 3を通過 した直後の低温冷媒と熱交換されるので、 熱交換を確実に行わせることができ、 しかも、 冷媒調整容器 3 0には冷媒量調整用のヒータ Hを付設したので、 このヒ ータ Hにて冷媒調整容器 3 0の温度を調整することができる。 このため、 冷凍サ ィクルを各季節に応じた冷媒循環量にて確実に運転することができる。 すなわち、 この場合、 低温冷媒との熱交換と、 ヒータ Hの加熱とにより外気温度に依存して 変化する温度環境を構成している。 With the configuration as shown in FIG. 4, the refrigerant in the refrigerant adjustment container 30 exchanges heat with the low-temperature refrigerant immediately after passing through the throttle 33, so that the heat exchange can be reliably performed. Since the refrigerant adjustment container 30 is provided with a heater H for adjusting the amount of refrigerant, the heater H can adjust the temperature of the refrigerant adjustment container 30. For this reason, the refrigeration cycle can be reliably operated with the refrigerant circulation amount corresponding to each season. That is, in this case, a temperature environment that changes depending on the outside air temperature is formed by heat exchange with the low-temperature refrigerant and heating of the heater H.
外気温度に依存して変化する温度環境下に置く他の方法として次の場合がある。 例えば、 冷媒調整容器 3 0を単に、 外気にさらされる位置 (例えば、 この冷凍サ ィクルが収納されるケーシングの外部) に配置する。 この場合、 外気に冷媒調整 容器 3 0がさらされれば、 この冷媒調整容器 3 0はその外気の温度に応じて暖め られたり、 冷やされたりすることになる。 また、 蒸発器 1 8にはファン 4◦が付 設されるので、 このファン 4 0にて生じる風通路内に冷媒調整容器 3 0を配置す る。 この場合、 蒸発器 1 8の上流の風上であっても、 蒸発器 1 8の上流の風下で あってもよレ、。 この場合も、 この風通路内の温度が外気に依存するからである。 特に、 熱交換上、 冷媒調整容器 3 0を蒸発器 1 8よりも下流の風下側に配置する のが好ましい。 さらには、 ペルチェ素子等を使用してもよい。 ここで、 ぺ^/チェ 素子とは、 異種の導体 (または半導体) の接点に電流を通すとき、 接点でジユー ノレ熱以外に熱の発生または吸収が起こる現象であるペルチェ効果を発揮すること ができる素子である。 従って、 この場合、 上記外気温度サーミスタ 3 8にて外気 温度を検知 (検出) して、 この外気温度に基づいて、 冷媒調整容器 3 0に対して ペルチェ素子を発熱 *吸熱させる。 また、 冷媒調整容器 3 0を水と熱交換するよ うにしてもよレ、。 この場合、 冷却用の水としては、 市水 (水道水) や、 貯湯タン ク 3の取水口 7から循環路 9へ流出した水等にて構成することができる。 巿水Other methods for placing the device under a temperature environment that varies depending on the outside air temperature include the following. For example, the refrigerant adjustment container 30 is simply arranged at a position exposed to the outside air (for example, outside the casing in which the frozen cycle is stored). In this case, if the refrigerant adjustment container 30 is exposed to the outside air, the refrigerant adjustment container 30 is heated or cooled according to the temperature of the outside air. Further, since the evaporator 18 is provided with a fan 4 °, the refrigerant adjusting container 30 is arranged in an air passage formed by the fan 40. In this case, either upstream of the evaporator 18 or downstream of the evaporator 18. Also in this case, the temperature in the air passage depends on the outside air. In particular, for heat exchange, it is preferable to arrange the refrigerant regulating container 30 on the leeward side downstream of the evaporator 18. Further, a Peltier element or the like may be used. Here, the ぺ ^ / che element means that when current flows through the contacts of different types of conductors (or semiconductors), This element can exhibit the Peltier effect, which is a phenomenon that generates or absorbs heat in addition to the heat generated. Therefore, in this case, the outside air temperature is detected (detected) by the outside air temperature thermistor 38, and the Peltier element is caused to generate heat * by the refrigerant adjustment container 30 based on the outside air temperature. Further, the refrigerant adjustment container 30 may be configured to exchange heat with water. In this case, the cooling water can be composed of city water (tap water), water flowing out from the intake port 7 of the hot water storage tank 3 to the circulation path 9, and the like. Water
(水道水) を使用する場合は、 貯湯タンク 3に水道水を供給する水道管に冷媒調 整容器 3 0を付設すればよく、 循環路 9の水を使用する場合は、 貯湯タンク 3の 取水口 7とガス冷却器 1 6の入口との間の配管に冷媒調整容器 3 0を付設すれば よい。 When using (tap water), it is only necessary to attach a refrigerant regulating container 30 to the water pipe that supplies tap water to the hot water storage tank 3.When using water from the circulation path 9, water is taken from the hot water storage tank 3. What is necessary is just to attach the refrigerant adjustment container 30 to the pipe between the port 7 and the inlet of the gas cooler 16.
以上にこの発明の具体的な実施の形態について説明したが、 この発明は上記形 態に限定されるものではなく、 この発明の範囲内で種々変更して実施することが できる。 例えば、 冷媒調整容器 3 0を蒸発器出口から圧縮機吸入口に至る冷媒配 管 2 4に配置する場合、 液ガス熱交換器 2 7の第 2通路 2 9よりも蒸発器 1 8側 に配置することも可能である。 また、 絞り 3 3を介設しないものであっても、 液 ガス熱交換器 2 7を配置しないものであってもよい。 なお、 この冷凍サイクルと しては、 ヒートポンプ式給湯機以外の空調装置やショーケース等の各種の冷凍装 置に使用することが可能であり、 また、 冷媒としては、 炭酸ガス以外に、 ェチレ ンゃェタン、 酸化窒素等の超臨界で使用する冷媒であってもよく、 さらには、 超 臨界で使用する冷媒ではなく、 ジクロロジフルォロメタン (R—1 2 ) やクロ口 ジフルォロメタン (R— 2 2 ) のような冷媒を使用してもよレ、。 Although the specific embodiments of the present invention have been described above, the present invention is not limited to the above embodiments, and can be implemented with various modifications within the scope of the present invention. For example, when the refrigerant regulating container 30 is disposed in the refrigerant conduit 24 extending from the evaporator outlet to the compressor inlet, the refrigerant regulating container 30 is disposed closer to the evaporator 18 than the second passage 29 of the liquid-gas heat exchanger 27. It is also possible. Further, it may be either a structure without the throttle 33 or a structure without the liquid-gas heat exchanger 27. This refrigeration cycle can be used in various refrigeration systems such as air conditioners and showcases other than heat pump water heaters. In addition to carbon dioxide, refrigerants include ethylene. It may be a refrigerant used in supercritical conditions such as petane or nitric oxide. In addition, instead of the refrigerant used in supercritical conditions, dichlorodifluoromethane (R- 12) and chloro difluoromethane (R- 22) ).
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2003252242A AU2003252242A1 (en) | 2002-07-23 | 2003-07-23 | Refrigerating cycle |
| EP03765359A EP1541939A4 (en) | 2002-07-23 | 2003-07-23 | REFRIGERATION CYCLE |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002-213624 | 2002-07-23 | ||
| JP2002213624A JP3963134B2 (en) | 2002-07-23 | 2002-07-23 | Refrigeration cycle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2004010060A1 true WO2004010060A1 (en) | 2004-01-29 |
Family
ID=30767843
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2003/009319 Ceased WO2004010060A1 (en) | 2002-07-23 | 2003-07-23 | Refrigerating cycle |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP1541939A4 (en) |
| JP (1) | JP3963134B2 (en) |
| AU (1) | AU2003252242A1 (en) |
| WO (1) | WO2004010060A1 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012007864A (en) * | 2010-06-28 | 2012-01-12 | Mitsubishi Electric Corp | Liquid receiver and refrigerating cycle device using the same |
| WO2023166724A1 (en) | 2022-03-04 | 2023-09-07 | 三菱電機株式会社 | Refrigeration cycle device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6162757A (en) * | 1984-08-31 | 1986-03-31 | 三菱電機株式会社 | heating device |
| JPH0414975U (en) * | 1990-05-25 | 1992-02-06 | ||
| WO1999008053A1 (en) * | 1997-08-12 | 1999-02-18 | Zexel Corporation | Cooling cycle |
| JP2000179958A (en) * | 1998-12-16 | 2000-06-30 | Matsushita Electric Ind Co Ltd | Air conditioner |
| JP2002115924A (en) * | 2000-07-31 | 2002-04-19 | Daikin Ind Ltd | Heat pump type hot water heater apparatus |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2715317A (en) * | 1955-01-03 | 1955-08-16 | Robert L Rhodes | Automatic load control for a reversible heat pump and air conditioner |
| US3163015A (en) * | 1963-05-29 | 1964-12-29 | Gen Electric | Refrigeration system including charge checking means |
| US3191397A (en) * | 1963-07-23 | 1965-06-29 | Gen Electric | Refrigeration system including charge checking means |
| JPS6089627A (en) * | 1983-10-21 | 1985-05-20 | Mitsubishi Electric Corp | heating device |
| US4546616A (en) * | 1984-02-24 | 1985-10-15 | Carrier Corporation | Heat pump charge optimizer |
| US5611211A (en) * | 1994-09-07 | 1997-03-18 | General Electric Company | Refirgeration system with electrically controlled refrigerant storage device |
| JP3475203B2 (en) * | 1996-07-04 | 2003-12-08 | 株式会社鷺宮製作所 | Superheat control device for capillary tube |
| JP2000266415A (en) * | 1999-03-15 | 2000-09-29 | Bosch Automotive Systems Corp | Refrigerating cycle |
| JP2000346472A (en) * | 1999-06-08 | 2000-12-15 | Mitsubishi Heavy Ind Ltd | Supercritical steam compression cycle |
| JP3990524B2 (en) * | 2000-01-28 | 2007-10-17 | 株式会社前川製作所 | Compressive refrigeration unit for subcritical and supercritical operation |
-
2002
- 2002-07-23 JP JP2002213624A patent/JP3963134B2/en not_active Expired - Fee Related
-
2003
- 2003-07-23 EP EP03765359A patent/EP1541939A4/en not_active Withdrawn
- 2003-07-23 AU AU2003252242A patent/AU2003252242A1/en not_active Abandoned
- 2003-07-23 WO PCT/JP2003/009319 patent/WO2004010060A1/en not_active Ceased
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6162757A (en) * | 1984-08-31 | 1986-03-31 | 三菱電機株式会社 | heating device |
| JPH0414975U (en) * | 1990-05-25 | 1992-02-06 | ||
| WO1999008053A1 (en) * | 1997-08-12 | 1999-02-18 | Zexel Corporation | Cooling cycle |
| JP2000179958A (en) * | 1998-12-16 | 2000-06-30 | Matsushita Electric Ind Co Ltd | Air conditioner |
| JP2002115924A (en) * | 2000-07-31 | 2002-04-19 | Daikin Ind Ltd | Heat pump type hot water heater apparatus |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP1541939A4 * |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2004053191A (en) | 2004-02-19 |
| EP1541939A4 (en) | 2008-04-23 |
| JP3963134B2 (en) | 2007-08-22 |
| AU2003252242A1 (en) | 2004-02-09 |
| EP1541939A1 (en) | 2005-06-15 |
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