WO2019019514A1 - System for automatic gas extraction and discharge - Google Patents
System for automatic gas extraction and discharge Download PDFInfo
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- WO2019019514A1 WO2019019514A1 PCT/CN2017/114417 CN2017114417W WO2019019514A1 WO 2019019514 A1 WO2019019514 A1 WO 2019019514A1 CN 2017114417 W CN2017114417 W CN 2017114417W WO 2019019514 A1 WO2019019514 A1 WO 2019019514A1
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- chamber
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- gas
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- temperature generator
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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
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
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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
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
- F25B43/04—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for withdrawing non-condensible gases
- F25B43/046—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for withdrawing non-condensible gases for sorption type systems
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Definitions
- the invention relates to the technical field of air conditioners, in particular to an automatic exhausting and exhausting system.
- the absorption type lithium bromide cold water chiller generates non-condensable gas (such as hydrogen) during normal operation and when the container leaks air, the vacuum inside the unit is reduced, and the unit output and efficiency are reduced.
- non-condensable gas such as hydrogen
- the non-condensable gas of the lower body absorber and the evaporator of the main body is usually extracted by siphoning or ejector, but the pressure of the high temperature generator and the low temperature generator is lower than atmospheric pressure, and the non-condensing property thereof is generated.
- the gas cannot be discharged automatically and can only be extracted by means of a vacuum pump. Due to the large amount of water vapor inside the unit during the operation of the unit, the vacuum pump oil is emulsified seriously, and its ability to evacuate is limited, and the ideal vacuum state cannot be achieved.
- high-temperature generators and low-temperature generators have high water vapor partial pressure and high temperature, and the vacuum pump cannot work, and often requires shutdown to perform vacuuming.
- the technical solution of the present invention is: an automatic exhausting and exhausting system, comprising an exhaust chamber, a pumping chamber and a gas-liquid separating chamber, wherein the exhaust chamber is connected to a low temperature generator and/or a condenser via a solenoid valve;
- the gas chamber is connected to the absorber via a pipeline;
- the gas-liquid separation chamber is respectively connected with the exhaust chamber and the pumping chamber pipeline;
- the liquid-liquid detecting chamber is provided with a liquid level detecting element.
- the design idea of the above scheme is: when the high temperature generator absorbs heat to generate steam into the water chamber and the heat exchange tube of the low temperature generator, the non-condensable gas (generated or leaked) in the high temperature generator is brought into the steam stream. In the water chamber of the low temperature generator, the gas in the water chamber of the low temperature generator is extracted, which is equivalent to extracting the gas in the high temperature generator. The non-condensable gas on the solution side of the low temperature generator is brought into the condenser along with the vapor stream evaporated by the low temperature generator, and the gas in the extraction condenser is equivalent to the gas in the low temperature generator.
- the technical solution only needs to connect the exhaust chamber to the low temperature generator and/or the condenser, and no need to connect the high temperature generator.
- the exhaust chamber is connected to the low temperature generator to discharge the high temperature generator together with the non-condensable gas in the low temperature generator; the exhaust chamber is connected to the condenser, and the low temperature generator can be discharged together with the non-condensable gas in the condenser.
- the internal pressure of the low temperature generator and the internal pressure of the condenser are larger than the pressure of the absorber.
- the present invention has the following advantages: full use of the inside of the low temperature generator and the internal pressure of the condenser are greater than the pressure of the absorber, so that the non-condensable gas automatically flows into the exhaust chamber through the pipeline, thus,
- the forced introduction without the need to add a siphon or ejector device not only simplifies the structure but also reduces costs.
- the exhaust chamber pipe is connected to an exhaust pump, and the exhaust chamber pipe is connected to the air pump.
- the air pump can quickly discharge the non-condensable gas in the exhaust chamber; the air pump can quickly discharge the non-condensable gas in the pumping chamber.
- the exhaust chamber is connected to the water chamber of the low temperature generator via a solenoid valve, and the pumping chamber is connected to the barrel of the absorber via a pipeline; or the exhaust chamber is connected to the cylinder of the condenser via a solenoid valve to pump air.
- the chamber is connected to the barrel of the absorber via a pipeline; or the exhaust chamber is connected to the water chamber of the low temperature generator via a solenoid valve, and the exhaust chamber is connected to the barrel of the condenser via another solenoid valve, and the pumping chamber is pipelined Connect the barrel of the absorber.
- the solenoid valve is opened by a program or manually for a short time to allow non-condensable gas and part of the water vapor to pass through and enter the exhaust chamber. Immediately close the solenoid valve to avoid excessive water vapor entering the exhaust chamber to damage the pressure balance of other parts of the unit, resulting in abnormal unit operation.
- the pumping chamber and the gas-liquid separation chamber are connected by an exhaust pipe, and one end of the suction pipe extends into the gas-liquid separation chamber, and the distance of the suction pipe from the bottom of the gas-liquid separation chamber is smaller than the distance between the liquid level detecting component and the gas-liquid separation chamber. The distance from the bottom.
- the air suction pipe is of a siphon type or an ejector type. This makes it easy to pump quickly.
- a vacuum valve is disposed between the exhaust chamber and the low temperature generator and/or the condenser to prevent vacuum leakage inside the unit.
- the gas-liquid separation chamber is connected to the absorber through a return pipe. In this way, the lithium bromide solution in the gas-liquid separation chamber can be refluxed into the absorber for recycling.
- liquid level detecting element is connected to the controller, and the output end of the controller is connected to the electromagnetic valve, the exhaust pump and the air pump.
- an exhaust valve is further disposed on the exhaust chamber.
- an exhaust probe is further disposed on the exhaust chamber.
- the invention has the advantages that on the one hand, the inside of the low temperature generator and the internal pressure of the condenser are both larger than the pressure of the absorber, so that the non-condensable gas can automatically flow into the exhaust chamber through the pipeline, so that there is no need to add siphon or
- the forced introduction of the ejector device not only simplifies the structure but also reduces the cost; on the other hand, through the automatic control of the controller, the solenoid valve, the exhaust pump and the air pump, the inside of the low temperature generator water chamber and the inside of the condenser can be The non-condensable gas is pumped out and no vacuum pump is needed, which greatly reduces the cost.
- the high temperature generator and the low temperature generator have high temperature and high water vapor pressure. It is not suitable for vacuum pumping (causing vacuum pump oil emulsification or even vacuum pump destruction), nor can it ventilate the unit exhaust chamber and other positions for a long time (causing other The pressure of the part rises, and the evaporation and absorption are stopped.
- the present invention temporarily opens the electromagnetic valve by program control or manual operation, so that the air is not condensed. The gas and part of the water vapor are discharged into the exhaust chamber, the solenoid valve is closed, and the exhaust of the unit is completed by the exhaust pump. Therefore, it is possible to remove the non-condensable gas of the high temperature generator and the low temperature generator portion in the case of continuous startup operation.
- the present invention is compared with a method of extracting a non-condensable gas by a vacuum pump. Because the method of extruding the exhaust gas by the solution, only the non-condensable gas is excluded, and the water vapor, octanol or the like is not extracted by the vacuum pump, and the composition change of the solution is affected.
- FIG. 1 is a schematic structural view of an embodiment of the present invention.
- an automatic exhaust system includes an exhaust chamber 1, an exhaust chamber 2, and a gas-liquid separation chamber 3.
- the exhaust chamber 1 is connected to the water chamber of the low temperature generator via a solenoid valve 11 , and the exhaust chamber 1 is connected to the cylinder of the condenser via another electromagnetic valve 12 , and the pumping chamber 2 is connected to the barrel of the absorber via a pipeline.
- the gas-liquid separation chamber 3 is in communication with the exhaust chamber 1 and the pumping chamber 2, respectively; and the liquid-liquid detecting chamber 3 is provided with a liquid level detecting probe 4.
- the pumping chamber 2 is connected to the gas-liquid separation chamber 3 through the exhaust pipe 21, and one end of the exhaust pipe 21 extends into the gas-liquid separation chamber 3.
- the distance between the exhaust pipe 21 and the bottom of the gas-liquid separation chamber 3 is less than the liquid level detection.
- the distance of the needle 4 from the bottom of the gas-liquid separation chamber 3, one end of the suction pipe 21 extends into the pumping chamber 2, and the suction pipe 21 is a siphon type air pipe.
- the exhaust chamber 1 and the gas-liquid separation chamber 3 communicate with each other through an exhaust pipe 16.
- the exhaust chamber 1 is connected to an exhaust pump 5, and the exhaust chamber 2 is connected to an air pump 6.
- the gas-liquid separation chamber 3 is connected to the absorber through a return pipe 31.
- a manual vacuum valve 13 is also provided between the exhaust chamber 1 and the low temperature generator and the condenser, respectively.
- An exhaust valve 14 and an exhaust probe 15 are also provided on the exhaust chamber 1. When the pressure in the exhaust chamber 1 is greater than the external pressure, the exhaust valve 14 is automatically opened, and when the pressure in the exhaust chamber is lower than the external pressure, the exhaust valve 14 is automatically closed.
- the exhaust probe 15 can be used to display the magnitude of the pressure within the exhaust chamber 1.
- the liquid level detecting probe 4 is connected to the controller, and the output end of the controller is connected to a solenoid valve, an exhaust pump, and an air pump.
- the controller is preferably a PLC controller.
- the air pump 5 and the exhaust pump 6 are shielded pumps.
- the exhaust system is automatically exhausted intermittently, for example, once every 1 minute.
- the PLC controller controls the two solenoid valves to open. Since the absorption type lithium bromide cold warm water unit is in normal operation, the internal pressure of the low temperature generator and the internal pressure of the condenser are greater than the pressure of the absorber.
- a feature is that under the action of the pressure difference, the non-condensable gas from the high temperature generator automatically enters the exhaust chamber through the pipe connected to the low temperature generator, and the non-condensable gas from the low temperature generator automatically enters the exhaust through the pipe connected to the condenser.
- the non-condensable gas enters the gas-liquid separation chamber through the exhaust pipe, and the lithium bromide solution from the absorber is stored in the gas-liquid separation chamber, and the non-condensable gas is located on the upper side of the solution.
- the gas-liquid separation chamber is in communication with the pumping chamber, and the solution can be introduced into the pumping chamber; and the pump is always in operation, and the non-condensable gas in the pumping chamber is exhausted through the exhaust pipe. Inhalation of the gas-liquid separation chamber, the non-condensable gas is separated from the liquid, and the non-condensable gas is located on the upper side of the gas-liquid separation chamber.
- the liquid level detecting probe detects that the liquid level leaves the probe, and sends a signal.
- the controller controls the two solenoid valves to close, and quickly starts the exhaust pump to discharge the non-condensable gas out of the unit, that is, the non-condensable gas is discharged through the exhaust valve; when the liquid level detecting probe detects the liquid level, The controller controls the exhaust pump to stop venting.
- the embodiment can fully utilize the characteristics that the internal pressure of the low-temperature generator and the internal pressure of the condenser are larger than the pressure of the absorber, so that the non-condensable gas automatically flows into the exhaust chamber through the pipeline, so that it is not necessary to join.
- the forced introduction of the siphon or ejector device not only simplifies the structure but also reduces the cost; on the other hand, through the automatic control of the controller, solenoid valve, exhaust pump and air pump, the inside of the low temperature generator water chamber can be condensed The non-condensable gas inside the device is extracted, and no vacuum pump is needed, which greatly reduces the cost.
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- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Power Engineering (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
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Abstract
Description
本发明涉及空调技术领域,特别是一种自动抽排气系统。The invention relates to the technical field of air conditioners, in particular to an automatic exhausting and exhausting system.
吸收式溴化锂冷温水机组在正常运行过程中会产生不凝性气体(如氢气)以及容器泄漏空气进入时,均导致机组内部真空度下降,机组出力和效率降低。The absorption type lithium bromide cold water chiller generates non-condensable gas (such as hydrogen) during normal operation and when the container leaks air, the vacuum inside the unit is reduced, and the unit output and efficiency are reduced.
现有技术中,通常是采用虹吸或者引射的方式抽取主体下筒体吸收器和蒸发器的不凝性气体,但高温发生器和低温发生器的压力低于大气压,其产生的不凝性气体不能自动排出,只能依靠真空泵抽出。由于机组运行过程中,机组内部存在大量的水蒸气,会导致真空泵油乳化严重,其抽真空的能力受到限制,不能达到理想的真空状态。特别是高温发生器和低温发生器,其水蒸气分压高、温度高,真空泵无法工作,往往需要停机才能进行抽真空。In the prior art, the non-condensable gas of the lower body absorber and the evaporator of the main body is usually extracted by siphoning or ejector, but the pressure of the high temperature generator and the low temperature generator is lower than atmospheric pressure, and the non-condensing property thereof is generated. The gas cannot be discharged automatically and can only be extracted by means of a vacuum pump. Due to the large amount of water vapor inside the unit during the operation of the unit, the vacuum pump oil is emulsified seriously, and its ability to evacuate is limited, and the ideal vacuum state cannot be achieved. In particular, high-temperature generators and low-temperature generators have high water vapor partial pressure and high temperature, and the vacuum pump cannot work, and often requires shutdown to perform vacuuming.
发明内容Summary of the invention
本发明的目的是克服现有技术的上述不足而提供一种操作简单,成本低廉的自动抽排气系统。SUMMARY OF THE INVENTION It is an object of the present invention to provide an automatic exhaust system which is simple in operation and low in cost, overcoming the above-mentioned deficiencies of the prior art.
本发明的技术方案是:一种自动抽排气系统,包括排气室、抽气室和气液分离室,所述排气室经电磁阀管道连接低温发生器和/或冷凝器;所述抽气室经管道连接吸收器;所述气液分离室分别与排气室、抽气室管道连通;所述气液分离室内设有液位检测元件。The technical solution of the present invention is: an automatic exhausting and exhausting system, comprising an exhaust chamber, a pumping chamber and a gas-liquid separating chamber, wherein the exhaust chamber is connected to a low temperature generator and/or a condenser via a solenoid valve; The gas chamber is connected to the absorber via a pipeline; the gas-liquid separation chamber is respectively connected with the exhaust chamber and the pumping chamber pipeline; and the liquid-liquid detecting chamber is provided with a liquid level detecting element.
上述方案的设计思路为:当高温发生器在吸收热量产生蒸汽进入低温发生器的水室及换热管内时,高温发生器内(产生或漏入)的不凝性气体会被蒸汽流带入低温发生器的水室内,因此抽取低温发生器水室内的气体,也就相当于抽取高温发生器内的气体。而低温发生器溶液侧的不凝性气体会随低温发生器蒸发的蒸汽流带入冷凝器,抽取冷凝器内的气体也就相当于抽取低温发生器中的气体。因此,本技术方案只需将排气室与低温发生器和/或冷凝器相连即可,无需再连接高温发生器。排气室连接低温发生器,可将高温发生器连同低温发生器内的不凝性气体排出;排气室连接冷凝器,可将低温发生器连同冷凝器内的不凝性气体排出。The design idea of the above scheme is: when the high temperature generator absorbs heat to generate steam into the water chamber and the heat exchange tube of the low temperature generator, the non-condensable gas (generated or leaked) in the high temperature generator is brought into the steam stream. In the water chamber of the low temperature generator, the gas in the water chamber of the low temperature generator is extracted, which is equivalent to extracting the gas in the high temperature generator. The non-condensable gas on the solution side of the low temperature generator is brought into the condenser along with the vapor stream evaporated by the low temperature generator, and the gas in the extraction condenser is equivalent to the gas in the low temperature generator. Therefore, the technical solution only needs to connect the exhaust chamber to the low temperature generator and/or the condenser, and no need to connect the high temperature generator. The exhaust chamber is connected to the low temperature generator to discharge the high temperature generator together with the non-condensable gas in the low temperature generator; the exhaust chamber is connected to the condenser, and the low temperature generator can be discharged together with the non-condensable gas in the condenser.
另外,吸收式溴化锂冷温水机组在正常运行时,低温发生器内部和冷凝器内部压力均比吸收器压力大,利用这一特点,用管道将低温发生器或者冷凝器的不凝性气体引入机组的排气室,在压差下不凝性气体将通过管道自动流入排气室。In addition, in the normal operation of the absorption type lithium bromide cold water chiller, the internal pressure of the low temperature generator and the internal pressure of the condenser are larger than the pressure of the absorber. With this feature, the non-condensable gas of the low temperature generator or the condenser is introduced into the unit by the pipeline. The exhaust chamber, under the pressure difference, the non-condensable gas will automatically flow into the exhaust chamber through the pipeline.
因此,根据上述设计思路,本发明具有以下优点:充分利用低温发生器内部和冷凝器内部压力均比吸收器压力大这一特点,使不凝性气体通过管道自动流入排气室,这样,就无需加入虹吸或者引射式装置进行强制引入,不仅简化了结构,还降低了成本。 Therefore, according to the above design concept, the present invention has the following advantages: full use of the inside of the low temperature generator and the internal pressure of the condenser are greater than the pressure of the absorber, so that the non-condensable gas automatically flows into the exhaust chamber through the pipeline, thus, The forced introduction without the need to add a siphon or ejector device not only simplifies the structure but also reduces costs.
进一步,所述排气室管道连接排气泵,抽气室管道连接抽气泵。通过抽气泵,能够将排气室内的不凝性气体快速排出;通过抽气泵,可将抽气室内的不凝性气体快速排出。Further, the exhaust chamber pipe is connected to an exhaust pump, and the exhaust chamber pipe is connected to the air pump. The air pump can quickly discharge the non-condensable gas in the exhaust chamber; the air pump can quickly discharge the non-condensable gas in the pumping chamber.
进一步,所述排气室经一电磁阀管道连接低温发生器的水室,抽气室经管道连接吸收器的筒体;或者排气室经一电磁阀管道连接冷凝器的筒体,抽气室经管道连接吸收器的筒体;或者所述排气室经一电磁阀管道连接低温发生器的水室,排气室经另一电磁阀管道连接冷凝器的筒体,抽气室经管道连接吸收器的筒体。Further, the exhaust chamber is connected to the water chamber of the low temperature generator via a solenoid valve, and the pumping chamber is connected to the barrel of the absorber via a pipeline; or the exhaust chamber is connected to the cylinder of the condenser via a solenoid valve to pump air. The chamber is connected to the barrel of the absorber via a pipeline; or the exhaust chamber is connected to the water chamber of the low temperature generator via a solenoid valve, and the exhaust chamber is connected to the barrel of the condenser via another solenoid valve, and the pumping chamber is pipelined Connect the barrel of the absorber.
所述电磁阀通过程序控制或手动,短时间开启,使不凝性气体与部分水蒸气通过并进入排气室。旋即关闭电磁阀,避免过多的水蒸气进入排气室破坏机组其他部分的压力平衡,导致机组工作不正常。The solenoid valve is opened by a program or manually for a short time to allow non-condensable gas and part of the water vapor to pass through and enter the exhaust chamber. Immediately close the solenoid valve to avoid excessive water vapor entering the exhaust chamber to damage the pressure balance of other parts of the unit, resulting in abnormal unit operation.
进一步,所述抽气室与气液分离室之间通过抽气管连通,抽气管的一端伸入气液分离室,抽气管距离气液分离室底部的距离小于液位检测元件距离气液分离室底部的距离。这样,一方面便于将溶液压入抽气管进入抽气室内,直至液位检测元件检测到液位离开探针;另一方面,实现液封。Further, the pumping chamber and the gas-liquid separation chamber are connected by an exhaust pipe, and one end of the suction pipe extends into the gas-liquid separation chamber, and the distance of the suction pipe from the bottom of the gas-liquid separation chamber is smaller than the distance between the liquid level detecting component and the gas-liquid separation chamber. The distance from the bottom. Thus, on the one hand, it is convenient to press the solution into the suction pipe into the suction chamber until the liquid level detecting element detects that the liquid level leaves the probe; on the other hand, the liquid seal is realized.
进一步,所述抽气管为虹吸式或者引射式。这样,便于快速抽气。Further, the air suction pipe is of a siphon type or an ejector type. This makes it easy to pump quickly.
进一步,所述排气室与低温发生器和/或冷凝器之间还设有真空阀,可防止机组内的真空泄露。Further, a vacuum valve is disposed between the exhaust chamber and the low temperature generator and/or the condenser to prevent vacuum leakage inside the unit.
进一步,所述气液分离室通过回流管连接吸收器。这样,使得气液分离室内的溴化锂溶液能够回流至吸收器内进行循环利用。Further, the gas-liquid separation chamber is connected to the absorber through a return pipe. In this way, the lithium bromide solution in the gas-liquid separation chamber can be refluxed into the absorber for recycling.
进一步,所述液位检测元件连接控制器,控制器的输出端连接电磁阀、排气泵和抽气泵。通过控制器、电磁阀、排气泵和抽气泵的自动控制,能够将低温发生器水室内部和冷凝器内部的不凝性气体抽出,无需真空泵,大大降低成本。Further, the liquid level detecting element is connected to the controller, and the output end of the controller is connected to the electromagnetic valve, the exhaust pump and the air pump. Through the automatic control of the controller, solenoid valve, exhaust pump and air pump, the non-condensable gas inside the low temperature generator water chamber and the inside of the condenser can be extracted without a vacuum pump, which greatly reduces the cost.
进一步,所述排气室上还设有排气阀。Further, an exhaust valve is further disposed on the exhaust chamber.
进一步,所述排气室上还设有排气探针。Further, an exhaust probe is further disposed on the exhaust chamber.
本发明的有益效果:一方面能够充分利用低温发生器内部和冷凝器内部压力均比吸收器压力大这一特点,使不凝性气体通过管道自动流入排气室,这样,就无需加入虹吸或者引射式装置进行强制引入,不仅简化了结构,还降低了成本;另一方面,通过控制器、电磁阀、排气泵和抽气泵的自动控制,能够将低温发生器水室内部和冷凝器内部的不凝性气体抽出,无需真空泵,大大降低成本。The invention has the advantages that on the one hand, the inside of the low temperature generator and the internal pressure of the condenser are both larger than the pressure of the absorber, so that the non-condensable gas can automatically flow into the exhaust chamber through the pipeline, so that there is no need to add siphon or The forced introduction of the ejector device not only simplifies the structure but also reduces the cost; on the other hand, through the automatic control of the controller, the solenoid valve, the exhaust pump and the air pump, the inside of the low temperature generator water chamber and the inside of the condenser can be The non-condensable gas is pumped out and no vacuum pump is needed, which greatly reduces the cost.
由于机组运行时,高温发生器和低温发生器温度高,水蒸气压力高,既不宜真空泵抽气(导致真空泵油乳化甚至真空泵破坏),也不能长期对机组排气室及其他位置通气(导致其他部位气压上升,停止蒸发和吸收),本发明通过程序控制或手动,将电磁阀短暂开启,使不凝 性气体和部分水蒸气排入排气室后关闭电磁阀,并且通过排气泵完成对机组外排气。因此,可以在连续开机运行的情况下清除高温发生器和低温发生器部分的不凝性气体。Since the unit is running, the high temperature generator and the low temperature generator have high temperature and high water vapor pressure. It is not suitable for vacuum pumping (causing vacuum pump oil emulsification or even vacuum pump destruction), nor can it ventilate the unit exhaust chamber and other positions for a long time (causing other The pressure of the part rises, and the evaporation and absorption are stopped. The present invention temporarily opens the electromagnetic valve by program control or manual operation, so that the air is not condensed. The gas and part of the water vapor are discharged into the exhaust chamber, the solenoid valve is closed, and the exhaust of the unit is completed by the exhaust pump. Therefore, it is possible to remove the non-condensable gas of the high temperature generator and the low temperature generator portion in the case of continuous startup operation.
本发明与采用真空泵抽出不凝性气体的方法比较,因为采用溶液挤压排气的方法,只排除不凝性气体,而不会导致水蒸气、辛醇等被真空泵抽出,影响溶液成分变化。The present invention is compared with a method of extracting a non-condensable gas by a vacuum pump. Because the method of extruding the exhaust gas by the solution, only the non-condensable gas is excluded, and the water vapor, octanol or the like is not extracted by the vacuum pump, and the composition change of the solution is affected.
图1是本发明实施例的结构示意图。1 is a schematic structural view of an embodiment of the present invention.
以下将结合说明书附图和具体实施例对本发明做进一步详细说明。The invention will be further described in detail below in conjunction with the drawings and specific embodiments.
如图1所示:一种自动抽排气系统,包括排气室1、抽气室2和气液分离室3。排气室1经一电磁阀11管道连接低温发生器的水室,排气室1经另一电磁阀12管道连接冷凝器的筒体,抽气室2经管道连接吸收器的筒体。气液分离室3分别与排气室1、抽气室2管道连通;气液分离室3内设有液位检测探针4。其中,抽气室2与气液分离室3之间通过抽气管21连通,抽气管21的一端伸入气液分离室3,抽气管21距离气液分离室3底部的距离小于液位检测探针4距离气液分离室3底部的距离,抽气管21的一端伸入抽气室2内,抽气管21为虹吸式气管。排气室1与气液分离室3之间通过排气管16连通。As shown in FIG. 1, an automatic exhaust system includes an
排气室1管道连接排气泵5,抽气室2管道连接抽气泵6。气液分离室3通过回流管31连接吸收器。The
排气室1与低温发生器和冷凝器之间还分别设有手动真空阀13。排气室1上还设有排气阀14和排气探针15。当排气室1内的压力大于外界压力时,排气阀14会自动打开,当排气室内的压力低于外界压力时,排气阀14会自动关闭。排气探针15可用于显示排气室1内的压力大小。A
液位检测探针4连接控制器,控制器的输出端连接电磁阀、排气泵和抽气泵。本实施例中,控制器优选为PLC控制器。抽气泵5和排气泵6为屏蔽泵。The liquid
本实施例的工作原理时,通过对PLC控制器定时,使得本抽排气系统间歇式进行自动抽排气,如每隔1分钟抽排气一次。当抽排气设定时间到后,PLC控制器控制两个电磁阀开启,由于吸收式溴化锂冷温水机组在正常运行时,低温发生器内部和冷凝器内部压力均比吸收器压力大,利用这一特点,在压差作用下,来自高温发生器的不凝性气体经连接低温发生器的管道自动进入排气室,来自低温发生器的不凝性气体经连接冷凝器的管道自动进入排气室,由于排气室与气液分离室连通,不凝性气体通过排气管还进入气液分离室,气液分离室内储存有来自吸收器的溴化锂溶液,不凝性气体位于溶液的上侧,而气液分离室又与抽气室连通,可将溶液导入抽气室内;而抽气泵一直处于运行状态,通过抽气管将抽气室内的不凝性气体 吸入气液分离室,不凝性气体与液体分离,不凝性气体位于气液分离室的上侧,当气体压力增大,使得液位检测探针检测到液位离开探针时,发送信号给控制器,控制器控制两个电磁阀关闭,并迅速启动排气泵,将不凝性气体排出机组,即不凝性气体经排气阀排出;当液位检测探针检测到液位时,控制器控制排气泵停止排气。In the working principle of the embodiment, by timing the PLC controller, the exhaust system is automatically exhausted intermittently, for example, once every 1 minute. When the exhausting and exhausting time is set, the PLC controller controls the two solenoid valves to open. Since the absorption type lithium bromide cold warm water unit is in normal operation, the internal pressure of the low temperature generator and the internal pressure of the condenser are greater than the pressure of the absorber. A feature is that under the action of the pressure difference, the non-condensable gas from the high temperature generator automatically enters the exhaust chamber through the pipe connected to the low temperature generator, and the non-condensable gas from the low temperature generator automatically enters the exhaust through the pipe connected to the condenser. In the chamber, since the exhaust chamber is in communication with the gas-liquid separation chamber, the non-condensable gas enters the gas-liquid separation chamber through the exhaust pipe, and the lithium bromide solution from the absorber is stored in the gas-liquid separation chamber, and the non-condensable gas is located on the upper side of the solution. The gas-liquid separation chamber is in communication with the pumping chamber, and the solution can be introduced into the pumping chamber; and the pump is always in operation, and the non-condensable gas in the pumping chamber is exhausted through the exhaust pipe. Inhalation of the gas-liquid separation chamber, the non-condensable gas is separated from the liquid, and the non-condensable gas is located on the upper side of the gas-liquid separation chamber. When the gas pressure is increased, the liquid level detecting probe detects that the liquid level leaves the probe, and sends a signal. To the controller, the controller controls the two solenoid valves to close, and quickly starts the exhaust pump to discharge the non-condensable gas out of the unit, that is, the non-condensable gas is discharged through the exhaust valve; when the liquid level detecting probe detects the liquid level, The controller controls the exhaust pump to stop venting.
综上所述,本实施例一方面能够充分利用低温发生器内部和冷凝器内部压力均比吸收器压力大这一特点,使不凝性气体通过管道自动流入排气室,这样,就无需加入虹吸或者引射式装置进行强制引入,不仅简化了结构,还降低了成本;另一方面,通过控制器、电磁阀、排气泵和抽气泵的自动控制,能够将低温发生器水室内部和冷凝器内部的不凝性气体抽出,无需真空泵,大大降低成本。 In summary, the embodiment can fully utilize the characteristics that the internal pressure of the low-temperature generator and the internal pressure of the condenser are larger than the pressure of the absorber, so that the non-condensable gas automatically flows into the exhaust chamber through the pipeline, so that it is not necessary to join. The forced introduction of the siphon or ejector device not only simplifies the structure but also reduces the cost; on the other hand, through the automatic control of the controller, solenoid valve, exhaust pump and air pump, the inside of the low temperature generator water chamber can be condensed The non-condensable gas inside the device is extracted, and no vacuum pump is needed, which greatly reduces the cost.
Claims (10)
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| JP2019530710A JP6986081B2 (en) | 2017-07-25 | 2017-12-04 | Automatic extraction and exhaust system |
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| CN201710608826.XA CN107178938B (en) | 2017-07-25 | 2017-07-25 | Automatic exhaust system |
| CN201710608826.X | 2017-07-25 |
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| JP (1) | JP6986081B2 (en) |
| CN (1) | CN107178938B (en) |
| WO (1) | WO2019019514A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110170197A (en) * | 2019-07-04 | 2019-08-27 | 辽宁蓝海川流流体控制设备有限公司 | A kind of clapboard type filter |
| WO2021168360A1 (en) | 2020-02-20 | 2021-08-26 | Illumina, Inc. | Bus network for artificial intelligence-based base caller |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107178938B (en) * | 2017-07-25 | 2023-02-03 | 远大空调有限公司 | Automatic exhaust system |
| KR102266912B1 (en) * | 2021-01-29 | 2021-06-18 | (주)월드이엔씨 | Apparatus and method for extracting by automatic in vacuum hot water boiler |
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| JP2006214698A (en) * | 2005-02-07 | 2006-08-17 | Sanyo Electric Co Ltd | Extraction device |
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Also Published As
| Publication number | Publication date |
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| CN107178938A (en) | 2017-09-19 |
| JP6986081B2 (en) | 2021-12-22 |
| CN107178938B (en) | 2023-02-03 |
| JP2020528534A (en) | 2020-09-24 |
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