CN110873486A - An absorption type solution defrosting system and air conditioner - Google Patents

An absorption type solution defrosting system and air conditioner Download PDF

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CN110873486A
CN110873486A CN201911205461.1A CN201911205461A CN110873486A CN 110873486 A CN110873486 A CN 110873486A CN 201911205461 A CN201911205461 A CN 201911205461A CN 110873486 A CN110873486 A CN 110873486A
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solution
absorption
generator
heat exchanger
condenser
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CN110873486B (en
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胡洪昊
王啸娟
孙瑞松
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Aux Air Conditioning Co Ltd
Ningbo Aux Electric Co Ltd
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Ningbo Aux Electric Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
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Abstract

本发明提供一种吸收式溶液除霜系统,包括依次连接的吸收器、溶液泵、发生器和溶液冷凝器,其中,发生器设置在室内机换热器中,溶液冷凝器设置在室外机换热器中,吸收器中设有吸收式溶液;溶液泵可将吸收式溶液抽取至发生器中,发生器可利用室内机换热器的冷媒驱动蒸发吸收式溶液,蒸发后的气态的所述吸收式溶液可进入溶液冷凝器中。采用以上的系统后,本发明与现有技术相比具有以下优点:本发明的吸收式溶液除霜系统回路设置简单,利用吸收式溶液实现对室外机换热器的除霜,对空调器常规循环系统的影响较小;另一方面,利用室内机换热器的冷凝热作为驱动热源,不需要利用压缩机压缩冷媒,耗电少、溶液循环更加安全可靠。

Figure 201911205461

The invention provides an absorption type solution defrosting system, comprising an absorber, a solution pump, a generator and a solution condenser connected in sequence, wherein the generator is arranged in an indoor unit heat exchanger, and the solution condenser is arranged in an outdoor unit heat exchanger In the heater, the absorber is provided with an absorbing solution; the solution pump can pump the absorbing solution into the generator, and the generator can use the refrigerant of the indoor heat exchanger to drive the evaporating absorbing solution, and the vaporized gaseous The absorption solution can enter the solution condenser. After the above system is adopted, the present invention has the following advantages compared with the prior art: the circuit setting of the absorption type solution defrosting system of the present invention is simple, the absorption type solution is used to realize the defrosting of the outdoor unit heat exchanger, and the conventional The influence of the circulation system is small; on the other hand, the condensation heat of the indoor unit heat exchanger is used as the driving heat source, and the compressor does not need to be used to compress the refrigerant, so the power consumption is less, and the solution circulation is safer and more reliable.

Figure 201911205461

Description

一种吸收式溶液除霜系统及空调器An absorption type solution defrosting system and air conditioner

技术领域technical field

本发明涉及空调技术领域,具体而言,涉及一种吸收式溶液除霜系统及空调器。The invention relates to the technical field of air conditioners, in particular to an absorption type solution defrosting system and an air conditioner.

背景技术Background technique

空调器在冬季低温条件下运行制热模式时,冷凝器的盘管上常常会产生结霜现象,而随着霜层越来越厚,空调的制热效果也会越来越差,这时需进入化霜模式运行除霜。When the air conditioner operates in the heating mode under low temperature conditions in winter, frost often occurs on the coil of the condenser, and as the frost layer becomes thicker, the heating effect of the air conditioner will become worse and worse. Need to enter the defrost mode to run defrost.

现有技术的空调器在化霜运行期间,常用方法是机组利用四通换向阀换向将制热模式切换为制冷模式对室外机进行除霜,这种方法的缺点为:一方面,停机除霜影响空调制热能力;另一方面,四通换向阀频繁切换,产生噪音、影响其使用寿命。因此,现有技术中出现不停机除霜方法,包括一个制热回路和一个除霜回路的双通路,但该方法中除霜回路中利用的也是空调自身的冷凝剂,需要额外的换向阀反复切换,其回路设置、吸收式溶液除霜系统更为复杂,也容易对空调系统自身制热系统产生影响。During the defrosting operation of the air conditioner in the prior art, the common method is that the unit uses the four-way reversing valve to switch the heating mode to the cooling mode to defrost the outdoor unit. The disadvantages of this method are: on the one hand, the shutdown Defrost affects the heating capacity of the air conditioner; on the other hand, the four-way reversing valve switches frequently, which generates noise and affects its service life. Therefore, there is a non-stop defrosting method in the prior art, including a heating circuit and a double passage of a defrosting circuit, but in this method, the defrosting circuit also uses the condensing agent of the air conditioner itself, which requires an additional reversing valve Repeated switching will make the circuit setting and absorption solution defrosting system more complicated, and it is easy to affect the heating system of the air conditioning system itself.

发明内容SUMMARY OF THE INVENTION

本发明解决的问题是现有技术中双通路除霜方法的回路设置及控制复杂、易对空调系统自身制热系统产生影响的问题。The problem to be solved by the present invention is that the circuit setting and control of the dual-pass defrosting method in the prior art are complicated, and it is easy to affect the heating system of the air-conditioning system itself.

为解决上述问题,本发明第一方面提供一种吸收式溶液除霜系统,包括依次连接的吸收器、溶液泵、发生器和溶液冷凝器,其中,所述发生器设置在室内机换热器中,所述溶液冷凝器设置在室外机换热器中,所述吸收器中设有吸收式溶液;所述溶液泵可将所述吸收式溶液抽取至所述发生器中,所述发生器可利用室内机换热器的冷媒驱动蒸发所述吸收式溶液,蒸发后的气态的所述吸收式溶液可进入所述溶液冷凝器中。In order to solve the above problems, the first aspect of the present invention provides an absorption type solution defrosting system, including an absorber, a solution pump, a generator and a solution condenser connected in sequence, wherein the generator is arranged in the indoor unit heat exchanger. , the solution condenser is arranged in the outdoor heat exchanger, and the absorber is provided with an absorption solution; the solution pump can pump the absorption solution into the generator, and the generator The absorption type solution can be evaporated by the refrigerant drive of the indoor unit heat exchanger, and the evaporated gaseous absorption type solution can enter the solution condenser.

采用以上的系统后,本发明与现有技术相比具有以下优点:本发明的吸收式溶液除霜系统回路设置简单,利用吸收式溶液实现对室外机换热器的除霜,对空调器常规循环系统的影响较小;另一方面,利用室内机换热器的冷媒释放的冷凝热作为驱动热源,不需要利用压缩机压缩冷媒,耗电少、溶液循环更加安全可靠。After the above system is adopted, the present invention has the following advantages compared with the prior art: the circuit setting of the absorption type solution defrosting system of the present invention is simple, the absorption type solution is used to realize the defrosting of the outdoor unit heat exchanger, and the conventional The influence of the circulation system is small; on the other hand, the condensation heat released by the refrigerant of the indoor unit heat exchanger is used as the driving heat source, and the compressor does not need to be used to compress the refrigerant.

进一步的,所述发生器与所述溶液冷凝器之间设有储液罐;设置储液罐可使蒸发后的吸收式溶液实现充分的气液分离。Further, a liquid storage tank is arranged between the generator and the solution condenser; the liquid storage tank can be arranged to achieve sufficient gas-liquid separation of the evaporated absorption solution.

进一步的,所述吸收器与所述储液罐相连,所述储液罐中的液态吸收式溶液可流回所述吸收器中;采用上述结构,可使蒸发后的液体吸收式溶液回到吸收器中。Further, the absorber is connected to the liquid storage tank, and the liquid absorption solution in the liquid storage tank can flow back into the absorber; with the above structure, the evaporated liquid absorption solution can be returned to the absorber. in the absorber.

进一步的,所述吸收器与所述溶液冷凝器之间设有第一节流装置;可使溶液冷凝器冷凝后的吸收式溶液通过节流装置回到吸收器中。Further, a first throttling device is arranged between the absorber and the solution condenser; the absorption solution condensed by the solution condenser can be returned to the absorber through the throttling device.

进一步的,所述吸收式溶液除霜系统还包括辅助驱动热源,设置于所述发生器附近;设置辅助驱动热源可在室内机换热器的冷凝热无法驱动吸收式溶液蒸发时提供驱动热量。Further, the absorption solution defrosting system further includes an auxiliary driving heat source, which is arranged near the generator; the auxiliary driving heat source can provide driving heat when the condensation heat of the indoor unit heat exchanger cannot drive the evaporation of the absorption solution.

进一步的,所述辅助驱动热源为电加热装置;选用电加热装置成本低、控制简单。Further, the auxiliary driving heat source is an electric heating device; the selection of the electric heating device is low in cost and simple in control.

进一步的,所述发生器与所述室内机换热器并联设置,所述溶液冷凝器与所述室外机换热器并联设置;采用上述结构使得吸收式溶液除霜系统相对于空调制热系统独立,进一步减小对空调常规循环系统的影响。Further, the generator is arranged in parallel with the indoor unit heat exchanger, and the solution condenser is arranged in parallel with the outdoor unit heat exchanger; the above structure makes the absorption solution defrosting system relative to the air conditioning heating system. Independent, further reducing the impact on the conventional circulation system of the air conditioner.

进一步的,所述吸收式溶液包括高沸点工质和低沸点工质;利用低沸点和高沸点混合溶液,可提高换热效率,进而提高系统的除霜效率。Further, the absorption type solution includes a high-boiling point working fluid and a low-boiling point working fluid; using a mixed solution with a low boiling point and a high boiling point can improve the heat exchange efficiency, thereby improving the defrosting efficiency of the system.

进一步的,所述吸收式溶液可为氨水溶液、溴化锂水溶液或氯化钙-氨溶液。Further, the absorption solution can be an ammonia solution, a lithium bromide solution or a calcium chloride-ammonia solution.

本发明第二方面提供一种空调器,包括上述的吸收式溶液除霜系统。A second aspect of the present invention provides an air conditioner, comprising the above-mentioned absorption type solution defrosting system.

附图说明Description of drawings

图1为本发明实施例的吸收式溶液除霜系统和空调常规循环系统中各部件的连接关系示意图;Fig. 1 is the connection relation schematic diagram of each component in the absorption type solution defrosting system of the embodiment of the present invention and the air-conditioning conventional circulation system;

11-吸收器;12-溶液泵;13-发生器;14-储液罐;15-溶液冷凝器;16-第一节流装置;17-辅助驱动热源;21-室内机换热器;22-室外机换热器;23-第二节流装置;24-压缩机。11-absorber; 12-solution pump; 13-generator; 14-liquid storage tank; 15-solution condenser; 16-first throttling device; 17-auxiliary drive heat source; 21-indoor unit heat exchanger; 22 - outdoor unit heat exchanger; 23 - second throttling device; 24 - compressor.

具体实施方式Detailed ways

为使本发明的上述目的、特征和优点能够更为明显易懂,下面结合附图对本发明的具体实施例做详细的说明。In order to make the above objects, features and advantages of the present invention more clearly understood, the specific embodiments of the present invention will be described in detail below with reference to the accompanying drawings.

如图1所示,为本发明实施例的吸收式溶液除霜系统和空调常规循环系统中各部件的连接关系示意图,本发明实施例公开了一种吸收式溶液除霜系统,设置在空调器的运行系统中,空调器的运行系统中还包括常规空调循环系统,用于空调器的制冷制热循环,具体地,所述常规空调循环系统包括依次连接的压缩机24、室内机换热器21、第二节流装置23和室外机换热器22。As shown in FIG. 1, it is a schematic diagram of the connection relationship between the absorption type solution defrosting system according to the embodiment of the present invention and the various components in the air conditioner conventional circulation system. The embodiment of the present invention discloses an absorption type solution defrosting system, which is arranged in the air conditioner. In the operating system of the air conditioner, the operating system of the air conditioner also includes a conventional air conditioning circulation system for the refrigeration and heating cycle of the air conditioner. 21. The second throttling device 23 and the outdoor unit heat exchanger 22.

上述实施例中,所述吸收式溶液除霜系统,包括依次连接的吸收器11、溶液泵12、发生器13和溶液冷凝器15,其中,所述发生器13设置在所述室内机换热器21中,因此所述发生器13可利用所述室内机换热器21的冷凝热,所述冷凝热指的是室内机换热器21在制热工况下冷凝散热产生的热量;而所述溶液冷凝器15则设置在所述室外机换热器22中,因此,所述溶液冷凝器15冷凝放热,可对室外机换热器22实现除霜的效果。In the above embodiment, the absorption type solution defrosting system includes an absorber 11, a solution pump 12, a generator 13 and a solution condenser 15 connected in sequence, wherein the generator 13 is arranged in the indoor unit for heat exchange. Therefore, the generator 13 can utilize the condensation heat of the indoor unit heat exchanger 21, and the condensation heat refers to the heat generated by the condensation heat dissipation of the indoor unit heat exchanger 21 under heating conditions; and The solution condenser 15 is disposed in the outdoor unit heat exchanger 22 . Therefore, the solution condenser 15 condenses and releases heat, which can achieve the effect of defrosting the outdoor unit heat exchanger 22 .

优选地,所述发生器13与所述室内机换热器21并联设置,所述溶液冷凝器15与所述室外机换热器22并联设置,采用上述结构使得吸收式溶液除霜系统相对于空调制热系统独立,减小其对空调常规循环系统的影响。Preferably, the generator 13 is arranged in parallel with the indoor unit heat exchanger 21 , the solution condenser 15 is arranged in parallel with the outdoor unit heat exchanger 22 , and the above-mentioned structure makes the absorption solution defrosting system relatively The air-conditioning heating system is independent, reducing its impact on the conventional air-conditioning circulation system.

进一步的,所述吸收器11中设有吸收式溶液,所述溶液泵12可将所述吸收式溶液抽取至所述发生器13中,所述发生器13可利用室内机换热器21的冷凝热驱动蒸发所述吸收式溶液,蒸发后的气态吸收式溶液可进入所述溶液冷凝器15中。Further, the absorber 11 is provided with an absorption type solution, and the solution pump 12 can pump the absorption type solution into the generator 13, and the generator 13 can use the heat exchanger 21 of the indoor unit. The heat of condensation drives the evaporation of the absorption type solution, and the evaporated gaseous absorption type solution can enter the solution condenser 15 .

采用以上结构的系统后,本发明与现有技术相比具有以下优点:本发明的吸收式溶液除霜系统回路设置简单,利用吸收式溶液实现对室外机换热器的除霜,对空调常规循环系统的影响较小;另一方面,利用室内机换热器的冷媒释放的冷凝热作为驱动热源,不需要利用压缩机压缩冷媒,耗电少、溶液循环更加安全可靠;此外,该系统中不需要利用换向阀频繁换向,保证换向阀的使用寿命,一定程度上实现减少噪音。After adopting the above-structured system, the present invention has the following advantages compared with the prior art: the circuit setting of the absorption type solution defrosting system of the present invention is simple, the absorption type solution is used to realize the defrosting of the outdoor unit heat exchanger, the The influence of the circulation system is small; on the other hand, the condensation heat released by the refrigerant of the indoor unit heat exchanger is used as the driving heat source, and there is no need to use the compressor to compress the refrigerant, so the power consumption is less, and the solution circulation is safer and more reliable; There is no need to use the reversing valve frequently to change direction, so as to ensure the service life of the reversing valve and reduce noise to a certain extent.

优选地,所述吸收式溶液包括高沸点工质和低沸点工质。在所述发生器13与所述溶液冷凝器15之间设有储液罐14,所述吸收器11也与所述储液罐14相连,同时,在所述吸收器11与所述溶液冷凝器15之间还设有第一节流装置16。Preferably, the absorption solution includes a high-boiling-point working medium and a low-boiling-point working medium. A liquid storage tank 14 is provided between the generator 13 and the solution condenser 15, and the absorber 11 is also connected to the liquid storage tank 14. At the same time, the absorber 11 is condensed with the solution A first throttling device 16 is also provided between the devices 15 .

具体地,所述吸收式溶液进入发生器13后,发生器13吸热蒸发所述吸收式溶液,使其形成气液混合物,而所述气液混合物进入所述储液罐14中,所述储液罐14可使蒸发后的吸收式溶液实现充分的气液分离,其中,低沸点工质形成的高温高压气体进入溶液冷凝器15中,而高沸点工质形成的液态吸收式溶液则又流回所述吸收器11中。Specifically, after the absorption type solution enters the generator 13, the generator 13 absorbs heat to evaporate the absorption type solution to form a gas-liquid mixture, and the gas-liquid mixture enters the liquid storage tank 14, and the The liquid storage tank 14 can realize sufficient gas-liquid separation of the evaporated absorption solution, wherein the high-temperature and high-pressure gas formed by the low-boiling-point working fluid enters the solution condenser 15, and the liquid absorption-type solution formed by the high-boiling-point working fluid is again. flows back into the absorber 11 .

进一步的,进入溶液冷凝器15中的所述高温高压气体被溶液冷凝器15冷凝为液态,这个过程中可实现放热并对室外机换热器22进行除霜,而冷凝后的吸收式溶液则通过第一节流装置16回到吸收器13中,完成一个完整的除霜循环。Further, the high-temperature and high-pressure gas entering the solution condenser 15 is condensed into a liquid state by the solution condenser 15. In this process, heat can be released and the outdoor heat exchanger 22 can be defrosted, and the condensed absorption solution Then it returns to the absorber 13 through the first throttling device 16 to complete a complete defrosting cycle.

以上,采用高沸点工质和低沸点工质混合的吸收式溶液,当低沸点工质的溶液冷凝后进入吸收器11中,被吸收器11中的高沸点工质的溶液吸收实现放热,这部分热量能够减少发生器13中驱动吸收式溶液蒸发所需的冷凝热,实现提高了换热效率,进而提高系统的除霜效率。Above, adopt the absorption type solution that the high boiling point working fluid and the low boiling point working fluid mix, when the solution of the low boiling point working fluid condenses and enters the absorber 11, is absorbed by the solution of the high boiling point working fluid in the absorber 11 to realize exothermic, This part of the heat can reduce the condensation heat required to drive the evaporation of the absorption type solution in the generator 13, thereby improving the heat exchange efficiency, thereby improving the defrosting efficiency of the system.

优选地,所述吸收式溶液根据具体的使用环境不同可为氨水溶液、溴化锂水溶液或氯化钙-氨溶液。Preferably, the absorption solution can be an ammonia solution, a lithium bromide solution or a calcium chloride-ammonia solution according to the specific use environment.

此外,所述吸收式溶液除霜系统还包括辅助驱动热源17,设置于所述发生器13附近,设置辅助驱动热源17可在室内机换热器21提供的冷凝热无法驱动吸收式溶液蒸发时提供额外的驱动热量。In addition, the absorption type solution defrosting system also includes an auxiliary driving heat source 17, which is arranged near the generator 13. The auxiliary driving heat source 17 can be provided when the condensation heat provided by the indoor unit heat exchanger 21 cannot drive the absorption type solution evaporation. Provides additional drive heat.

具体地,所述辅助驱动热源17为电加热装置,选用电加热装置成本低、控制简单。Specifically, the auxiliary driving heat source 17 is an electric heating device, and the selection of the electric heating device is low in cost and simple in control.

本发明还提供一种空调器,包括上述的吸收式溶液除霜系统,当空调器运行制热模式时或运行制热模式一定时间后,控制开启溶液泵12,使吸收器11中的吸收式溶液进入发生器13中蒸发,蒸发后的高温高压气体流入溶液冷凝器15中冷凝放热,实现对室外机换热器22的除霜。在上述过程中,吸收式溶液除霜系统实现不停机除霜,提高除霜状况下空调器的制热能力,进而提高用户使用的舒适性;此外,吸收式溶液除霜系统对空调常规循环系统的影响较小,还具有耗电少、溶液循环安全可靠的优点。The present invention also provides an air conditioner, which includes the above-mentioned absorption type solution defrosting system. When the air conditioner operates in the heating mode or after running the heating mode for a certain period of time, the solution pump 12 is controlled to be turned on, so that the absorption type solution in the absorber 11 is activated. The solution enters the generator 13 to evaporate, and the evaporated high-temperature and high-pressure gas flows into the solution condenser 15 to condense and release heat, so as to realize the defrosting of the outdoor unit heat exchanger 22 . In the above process, the absorption solution defrosting system realizes non-stop defrosting, which improves the heating capacity of the air conditioner under defrosting conditions, thereby improving the user's comfort; It also has the advantages of less power consumption and safe and reliable solution circulation.

虽然本发明披露如上,但本发明并非限定于此。任何本领域技术人员,在不脱离本发明的精神和范围内,均可作各种更动与修改,因此本发明的保护范围应当以权利要求所限定的范围为准。Although the present invention is disclosed above, the present invention is not limited thereto. Any person skilled in the art can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the protection scope of the present invention should be based on the scope defined by the claims.

Claims (10)

1. The absorption type solution defrosting system is characterized by comprising an absorber (11), a solution pump (12), a generator (13) and a solution condenser (15) which are sequentially connected, wherein the generator (13) is arranged in an indoor unit heat exchanger (21), the solution condenser (15) is arranged in an outdoor unit heat exchanger (22), and the absorber (11) is filled with absorption type solution; the solution pump (12) can pump the absorption solution into the generator (13), the generator (13) can drive the absorption solution to evaporate by using a refrigerant of an indoor unit heat exchanger (21), and the evaporated gaseous absorption solution can enter the solution condenser (15).
2. The absorption solution defrost system according to claim 2, wherein a liquid reservoir (14) is provided between the generator (13) and the solution condenser (15).
3. The absorption solution defrost system of claim 3 wherein said absorber (11) is connected to said reservoir (14) and liquid absorption solution in said reservoir (14) is returned to said absorber (11).
4. The absorption solution defrost system according to claim 1, characterized in that a first throttle device (16) is arranged between the absorber (11) and the solution condenser (15).
5. The absorption solution defrost system of claim 1 further comprising an auxiliary drive heat source (17) disposed adjacent the generator (13).
6. The absorption solution defrost system of claim 5 wherein the auxiliary drive heat source (17) is an electrical heating device.
7. The absorption solution defrost system of claim 1 wherein the generator (13) is arranged in parallel with the indoor heat exchanger (21) and the solution condenser (15) is arranged in parallel with the outdoor heat exchanger (22).
8. The absorption solution defrost system of claim 1 wherein the absorption solution includes a high boiling point working fluid and a low boiling point working fluid.
9. The absorption solution defrost system of claim 8 wherein the absorption solution may be an aqueous ammonia solution, an aqueous lithium bromide solution, or a calcium chloride-ammonia solution.
10. An air conditioner comprising the absorption solution defrost system of any one of claims 1-9.
CN201911205461.1A 2019-11-29 2019-11-29 Absorption type solution defrosting system and air conditioner Active CN110873486B (en)

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Publication number Priority date Publication date Assignee Title
CN201561564U (en) * 2009-11-06 2010-08-25 清华大学 A direct-fired air source absorption heat pump water heater
CN103090593A (en) * 2011-11-07 2013-05-08 北京科技大学 Heat pump cycle system, heat pump cycle method and vaporization system
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