CN117870208A - Low-temperature type air source heat pump experiment system - Google Patents
Low-temperature type air source heat pump experiment system Download PDFInfo
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- CN117870208A CN117870208A CN202410049242.3A CN202410049242A CN117870208A CN 117870208 A CN117870208 A CN 117870208A CN 202410049242 A CN202410049242 A CN 202410049242A CN 117870208 A CN117870208 A CN 117870208A
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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
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
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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
- F25B41/00—Fluid-circulation arrangements
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control valves
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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
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
- F25B41/42—Arrangements for diverging or converging flows, e.g. branch lines or junctions
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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
- F25B43/003—Filters
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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
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01M—TESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
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- G01M99/002—Thermal testing
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Abstract
Description
技术领域Technical Field
本发明属于空调热泵领域,具体地说,涉及一种低温型空气源热泵实验系统。The invention belongs to the field of air conditioning heat pumps, and in particular, relates to a low-temperature air source heat pump experimental system.
背景技术Background technique
热泵消耗少量的高品位电能或燃料的化学能,就可获得大量的所需热能,其制热系数总是大于一,其发展和推广使用对于缓解能源紧张、降低污染排放有着重要的现实意义。到目前为止已有很多学者对空气源热泵供热系统从各方面进行了研究,但大部分研究只有模拟分析,缺乏实验研究,系统在宽范围、多样性的实际工况和极寒工况下的运行情况尚未可知,这是因为现有的实验系统存在受环境条件影响大、实验成本高、研究内容单一、调节灵活性差、难以在低温工况下运行等问题。Heat pumps consume a small amount of high-quality electricity or chemical energy of fuel to obtain a large amount of required heat energy. Their heating coefficient is always greater than one. Their development and promotion have important practical significance for alleviating energy shortages and reducing pollution emissions. So far, many scholars have studied air source heat pump heating systems from various aspects, but most of the research is only simulation analysis, lack of experimental research, and the operation of the system under a wide range of diverse actual working conditions and extremely cold conditions is still unknown. This is because the existing experimental system is greatly affected by environmental conditions, has high experimental costs, single research content, poor adjustment flexibility, and is difficult to operate under low temperature conditions.
为此,提出一种低温型空气源热泵实验系统,以解决上述弊端。Therefore, a low-temperature air source heat pump experimental system is proposed to solve the above-mentioned drawbacks.
发明内容Summary of the invention
本发明要解决的技术问题在于克服现有技术的不足,提供一种低温型空气源热泵实验系统。The technical problem to be solved by the present invention is to overcome the deficiencies of the prior art and provide a low-temperature air source heat pump experimental system.
为解决上述技术问题,本发明采用技术方案的基本构思是:In order to solve the above technical problems, the basic concept of the technical solution adopted by the present invention is:
一种低温型空气源热泵实验系统,包括三个子系统,分别是一个空气源热泵系统、一个冷凝温度调节系统、一个蒸发温度调节系统;A low-temperature air source heat pump experimental system includes three subsystems, namely an air source heat pump system, a condensing temperature adjustment system, and an evaporation temperature adjustment system;
所述空气源热泵系统包括:压缩机、与所述压缩机相连接的冷凝器、与所述冷凝器相连接的干燥过滤器、与所述干燥过滤器相连接的节流阀、与所述节流阀相连接的蒸发器、与所述蒸发器相连接的气液分离器;The air source heat pump system comprises: a compressor, a condenser connected to the compressor, a drying filter connected to the condenser, a throttle valve connected to the drying filter, an evaporator connected to the throttle valve, and a gas-liquid separator connected to the evaporator;
所述冷凝温度调节系统包括:与所述冷凝器相连接的冷却水出口、与所述冷却水出口相连接的冷却水进口、与所述冷却水进口相连接的冷却水循环水泵;The condensing temperature regulating system comprises: a cooling water outlet connected to the condenser, a cooling water inlet connected to the cooling water outlet, and a cooling water circulation pump connected to the cooling water inlet;
所述蒸发温度调节系统包括:膨胀水箱、与所述膨胀水箱相连接的不锈钢水泵、与所述不锈钢水泵相连接的中间路换热器。The evaporation temperature regulating system comprises: an expansion water tank, a stainless steel water pump connected to the expansion water tank, and an intermediate heat exchanger connected to the stainless steel water pump.
可选的,在冷凝温度调节系统中,所述冷却水循环水泵进出口装设有第一旁通管路,所述第一旁通管路上装设有第一调节阀,所述冷却水进口上装设有第二调节阀,所述冷却水出口装设有第七调节阀,在蒸发温度调节系统中,所述蒸发器进口装设有第三调节阀,所述蒸发器进出口装设有第二旁通管路,所述第二旁通管路上装设有第四调节阀,所述中间路换热器进口装设有第五调节阀,所述中间路换热器进出口装设有第三旁通管路,所述第三旁通管路上装设有第六调节阀。Optionally, in the condensing temperature control system, the cooling water circulating water pump inlet and outlet are equipped with a first bypass pipeline, the first bypass pipeline is equipped with a first regulating valve, the cooling water inlet is equipped with a second regulating valve, and the cooling water outlet is equipped with a seventh regulating valve; in the evaporating temperature control system, the evaporator inlet is equipped with a third regulating valve, the evaporator inlet and outlet are equipped with a second bypass pipeline, the second bypass pipeline is equipped with a fourth regulating valve, the intermediate heat exchanger inlet is equipped with a fifth regulating valve, the intermediate heat exchanger inlet and outlet are equipped with a third bypass pipeline, and the third bypass pipeline is equipped with a sixth regulating valve.
可选的,所述冷却水循环水泵的出口与所述冷凝器的进口连通,所述冷却水循环水泵的进口经所述第一调节阀与所述冷却水循环水泵的出口连通构成所述第一旁通管路,所述冷凝器的出口经所述冷却水出口、冷却水进口与所述冷却水循环水泵的进口连通,所述冷却水进口与所述第二调节阀连通,所述冷却水出口与所述中间路换热器的进口连通,所述中间路换热器的出口与所述第七调节阀连通,所述第七调节阀控制所述冷凝器的冷凝温度,所述第一调节阀控制所述冷凝器的冷却水流量,同时调节所述第一调节阀和所述第七调节阀可模拟用户供暖负荷。Optionally, the outlet of the cooling water circulation pump is connected to the inlet of the condenser, and the inlet of the cooling water circulation pump is connected to the outlet of the cooling water circulation pump via the first regulating valve to form the first bypass pipeline, the outlet of the condenser is connected to the inlet of the cooling water circulation pump via the cooling water outlet and the cooling water inlet, the cooling water inlet is connected to the second regulating valve, the cooling water outlet is connected to the inlet of the intermediate heat exchanger, the outlet of the intermediate heat exchanger is connected to the seventh regulating valve, the seventh regulating valve controls the condensing temperature of the condenser, the first regulating valve controls the cooling water flow rate of the condenser, and adjusting the first regulating valve and the seventh regulating valve at the same time can simulate the user's heating load.
可选的,所述不锈钢水泵的出口经第五调节阀与中间路换热器的进口连通,所述第五调节阀的进口经所述第六调节阀与所述中间路换热器的出口连通构成所述第三旁通管路,所述中间路换热器的出口与经第三调节阀与蒸发器的进口连通,所述第三调节阀的进口经所述第四调节阀与所述蒸发器的出口连通构成所述第二旁通管路,所述蒸发器的出口经所述膨胀水箱与所述不锈钢水泵的进口连通,所述蒸发温度调节系统中的换热介质为乙二醇水溶液,所述第六调节阀控制所述蒸发器的蒸发温度,所述第三调节阀和所述第四调节阀控制进入所述蒸发器的乙二醇水溶液的质量流量,所述中间路换热器中换热介质的相对流向为顺流,所述第四调节阀控制进入所述中间路换热器的乙二醇水溶液的温度,所述第五调节阀和所述第六调节阀调节进入所述中间路换热器的乙二醇水溶液的质量流量。Optionally, the outlet of the stainless steel water pump is connected to the inlet of the intermediate heat exchanger via the fifth regulating valve, the inlet of the fifth regulating valve is connected to the outlet of the intermediate heat exchanger via the sixth regulating valve to form the third bypass pipeline, the outlet of the intermediate heat exchanger is connected to the inlet of the evaporator via the third regulating valve, the inlet of the third regulating valve is connected to the outlet of the evaporator via the fourth regulating valve to form the second bypass pipeline, the outlet of the evaporator is connected to the inlet of the stainless steel water pump via the expansion water tank, the heat exchange medium in the evaporation temperature regulation system is ethylene glycol aqueous solution, the sixth regulating valve controls the evaporation temperature of the evaporator, the third regulating valve and the fourth regulating valve control the mass flow rate of the ethylene glycol aqueous solution entering the evaporator, the relative flow direction of the heat exchange medium in the intermediate heat exchanger is downstream, the fourth regulating valve controls the temperature of the ethylene glycol aqueous solution entering the intermediate heat exchanger, and the fifth regulating valve and the sixth regulating valve regulate the mass flow rate of the ethylene glycol aqueous solution entering the intermediate heat exchanger.
采用上述技术方案后,本发明与现有技术相比具有以下有益效果,当然,实施本发明的任一产品并不一定需要同时达到以下所述的所有优点:After adopting the above technical solution, the present invention has the following beneficial effects compared with the prior art. Of course, any product implementing the present invention does not necessarily need to achieve all the advantages described below at the same time:
冷凝器、蒸发器和中间路换热器连接三个子系统,由中间路换热器平衡蒸发温度调节系统和冷凝温度调节系统的冷热负荷,通过合理的阀门调节方案,为空气源热泵系统中的蒸发器提供所需的低温室外温度工况,并保证进入冷凝器的冷却水温度稳定,使实验研究不再受室外气象条件限制并降低实验成本,具有安全便捷、经济性高、灵活性好等优点。The condenser, evaporator and intermediate heat exchanger connect three subsystems. The intermediate heat exchanger balances the cold and hot loads of the evaporation temperature regulation system and the condensation temperature regulation system. Through a reasonable valve adjustment scheme, the required low-temperature outdoor temperature working conditions are provided for the evaporator in the air source heat pump system, and the temperature of the cooling water entering the condenser is guaranteed to be stable, so that the experimental research is no longer restricted by outdoor meteorological conditions and the experimental cost is reduced. It has the advantages of safety, convenience, high economy and good flexibility.
下面结合附图对本发明的具体实施方式作进一步详细的描述。The specific implementation modes of the present invention are further described in detail below in conjunction with the accompanying drawings.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
下面描述中的附图仅仅是一些实施例,对于本领域普通技术人员来说,在不付出创造性劳动的前提下,还可以根据这些附图获得其他附图。在附图中:The drawings described below are only some embodiments. For those skilled in the art, other drawings can be obtained based on these drawings without creative work. In the drawings:
图1为本发明一实施例的低温型空气源热泵实验系统结构示意图。FIG1 is a schematic structural diagram of a low-temperature air source heat pump experimental system according to an embodiment of the present invention.
附图中,各标号所代表的部件列表如下:In the accompanying drawings, the components represented by the reference numerals are listed as follows:
压缩机1,冷凝器2,干燥过滤器3,节流阀4,蒸发器5,气液分离器6,冷却水循环水泵7,冷却水进口8,冷却水出口9,第一调节阀10,第二调节阀11,第一旁通管路12,膨胀水箱13,不锈钢水泵14,中间路换热器15,第三调节阀16,第四调节阀17,第五调节阀18,第六调节阀19,第七调节阀20,第二旁通管路21,第三旁通管路22。Compressor 1, condenser 2, drying filter 3, throttle valve 4, evaporator 5, gas-liquid separator 6, cooling water circulation pump 7, cooling water inlet 8, cooling water outlet 9, first regulating valve 10, second regulating valve 11, first bypass pipeline 12, expansion water tank 13, stainless steel water pump 14, intermediate heat exchanger 15, third regulating valve 16, fourth regulating valve 17, fifth regulating valve 18, sixth regulating valve 19, seventh regulating valve 20, second bypass pipeline 21, third bypass pipeline 22.
需要说明的是,这些附图和文字描述并不旨在以任何方式限制本发明的构思范围,而是通过参考特定实施例为本领域技术人员说明本发明的概念。It should be noted that these drawings and textual descriptions are not intended to limit the conceptual scope of the present invention in any way, but rather to illustrate the concept of the present invention for those skilled in the art by referring to specific embodiments.
实施方式Implementation
现在结合附图对本发明作进一步详细的说明。The present invention will now be described in further detail with reference to the accompanying drawings.
请参阅图1所示,在本实施例中提供了一种低温型空气源热泵实验系统,包括三个子系统,分别是一个空气源热泵系统、一个冷凝温度调节系统、一个蒸发温度调节系统;Please refer to FIG. 1 , in this embodiment, a low-temperature air source heat pump experimental system is provided, which includes three subsystems, namely, an air source heat pump system, a condensing temperature adjustment system, and an evaporation temperature adjustment system;
空气源热泵系统包括:压缩机1、与压缩机1相连接的冷凝器2、与冷凝器2相连接的干燥过滤器3、与干燥过滤器3相连接的节流阀4、与节流阀4相连接的蒸发器5、与蒸发器5相连接的气液分离器6;The air source heat pump system includes: a compressor 1, a condenser 2 connected to the compressor 1, a drying filter 3 connected to the condenser 2, a throttle valve 4 connected to the drying filter 3, an evaporator 5 connected to the throttle valve 4, and a gas-liquid separator 6 connected to the evaporator 5;
冷凝温度调节系统包括:与冷凝器2相连接的冷却水出口9、与冷却水出口9相连接的冷却水进口8、与冷却水进口8相连接的冷却水循环水泵7;The condensation temperature regulating system comprises: a cooling water outlet 9 connected to the condenser 2, a cooling water inlet 8 connected to the cooling water outlet 9, and a cooling water circulation pump 7 connected to the cooling water inlet 8;
蒸发温度调节系统包括:膨胀水箱13、与膨胀水箱13相连接的不锈钢水泵14、与不锈钢水泵14相连接的中间路换热器15。The evaporation temperature adjustment system includes: an expansion water tank 13 , a stainless steel water pump 14 connected to the expansion water tank 13 , and an intermediate heat exchanger 15 connected to the stainless steel water pump 14 .
冷凝器2、蒸发器5和中间路换热器15连接三个子系统,由中间路换热器15平衡蒸发温度调节系统和冷凝温度调节系统的冷热负荷,通过合理的阀门调节方案,为空气源热泵系统中的蒸发器提供所需的低温室外温度工况,并保证进入冷凝器的冷却水温度稳定,使实验研究不再受室外气象条件限制并降低实验成本。具有安全便捷、经济性高、灵活性好等优点。The condenser 2, evaporator 5 and intermediate heat exchanger 15 connect three subsystems. The intermediate heat exchanger 15 balances the cold and hot loads of the evaporation temperature regulation system and the condensation temperature regulation system. Through a reasonable valve regulation scheme, the required low-temperature outdoor temperature condition is provided for the evaporator in the air source heat pump system, and the temperature of the cooling water entering the condenser is ensured to be stable, so that the experimental research is no longer restricted by outdoor meteorological conditions and the experimental cost is reduced. It has the advantages of safety, convenience, high economy and good flexibility.
本实施例的在冷凝温度调节系统中,冷却水循环水泵7进出口装设有第一旁通管路12,第一旁通管路12上装设有第一调节阀10,冷却水进口8上装设有第二调节阀11,冷却水出口9装设有第七调节阀20,在蒸发温度调节系统中,蒸发器5进口装设有第三调节阀16,蒸发器5进出口装设有第二旁通管路21,第二旁通管路21上装设有第四调节阀17,中间路换热器15进口装设有第五调节阀18,中间路换热器15进出口装设有第三旁通管路22,第三旁通管路22上装设有第六调节阀19。In the condensing temperature regulating system of the present embodiment, a first bypass pipeline 12 is installed at the inlet and outlet of the cooling water circulating water pump 7, a first regulating valve 10 is installed on the first bypass pipeline 12, a second regulating valve 11 is installed on the cooling water inlet 8, and a seventh regulating valve 20 is installed on the cooling water outlet 9. In the evaporating temperature regulating system, a third regulating valve 16 is installed at the inlet of the evaporator 5, a second bypass pipeline 21 is installed at the inlet and outlet of the evaporator 5, a fourth regulating valve 17 is installed on the second bypass pipeline 21, a fifth regulating valve 18 is installed at the inlet of the intermediate heat exchanger 15, a third bypass pipeline 22 is installed at the inlet and outlet of the intermediate heat exchanger 15, and a sixth regulating valve 19 is installed on the third bypass pipeline 22.
本实施例的压缩机1的排气口与冷凝器2的进口连通,冷凝器2的出口经干燥过滤器3与节流阀4的进口连通,节流阀4的出口与蒸发器5的进口连通,蒸发器5的出口经气液分离器6与压缩机1的吸气口连通,从冷凝器2流出的液态制冷剂经干燥过滤器3在节流阀4中节流降压,然后进入蒸发器5中吸热气化,气态制冷剂经气液分离器6进入压缩机1的吸气口,压缩成高温高压的制冷剂,由压缩机1的排气口进入冷凝器2,在冷凝器2中向冷却水放热变成液态,进行下一个循环,由蒸发器5出口制冷剂的过热度控制节流阀4的开度,调节空气源热泵系统中循环制冷剂的质量流量,当过热度偏小时,减小节流阀4的开度;当过热度偏大时,增大节流阀4的开度。The exhaust port of the compressor 1 of the present embodiment is connected with the inlet of the condenser 2, the outlet of the condenser 2 is connected with the inlet of the throttle valve 4 via the drying filter 3, the outlet of the throttle valve 4 is connected with the inlet of the evaporator 5, the outlet of the evaporator 5 is connected with the air intake port of the compressor 1 via the gas-liquid separator 6, the liquid refrigerant flowing out of the condenser 2 is throttled and reduced in pressure in the throttle valve 4 via the drying filter 3, and then enters the evaporator 5 to absorb heat and vaporize, the gaseous refrigerant enters the air intake port of the compressor 1 via the gas-liquid separator 6, is compressed into a high-temperature and high-pressure refrigerant, enters the condenser 2 from the exhaust port of the compressor 1, releases heat to the cooling water in the condenser 2 to become liquid, and performs the next cycle, the opening of the throttle valve 4 is controlled by the superheat of the refrigerant at the outlet of the evaporator 5, and the mass flow rate of the circulating refrigerant in the air source heat pump system is adjusted, when the superheat is small, the opening of the throttle valve 4 is reduced; when the superheat is large, the opening of the throttle valve 4 is increased.
本实施例的冷却水循环水泵7的出口与冷凝器2的进口连通,冷却水循环水泵7的进口经第一调节阀10与冷却水循环水泵7的出口连通构成第一旁通管路12,冷凝器2的出口经冷却水出口9、冷却水进口8与冷却水循环水泵7的进口连通,冷却水进口8与第二调节阀11连通,冷却水出口9与中间路换热器15的进口连通,中间路换热器15的出口与第七调节阀20连通,第七调节阀20控制冷凝器2的冷凝温度,降低冷凝温度时,增大第七调节阀20的开度;提高冷凝温度时,则反之,以此保证进入冷凝器2的冷却水温度稳定,第一调节阀10控制冷凝器2的冷却水流量,降低冷凝器2中冷却水进出口温差时,增大第一调节阀10的开度,以此提高冷却水流量;提高冷凝器2中冷却水进出口温差时,则反之,同时调节第一调节阀10和第七调节阀20可模拟用户供暖负荷。The outlet of the cooling water circulation pump 7 of this embodiment is connected with the inlet of the condenser 2, and the inlet of the cooling water circulation pump 7 is connected with the outlet of the cooling water circulation pump 7 through the first regulating valve 10 to form a first bypass pipeline 12. The outlet of the condenser 2 is connected with the inlet of the cooling water circulation pump 7 through the cooling water outlet 9 and the cooling water inlet 8. The cooling water inlet 8 is connected with the second regulating valve 11. The cooling water outlet 9 is connected with the inlet of the intermediate heat exchanger 15. The outlet of the intermediate heat exchanger 15 is connected with the seventh regulating valve 20. The seventh regulating valve 20 controls the condensation temperature of the condenser 2. When the condensation temperature is reduced, the opening of the seventh regulating valve 20 is increased; when the condensation temperature is increased, the opening is increased, thereby ensuring that the temperature of the cooling water entering the condenser 2 is stable. The first regulating valve 10 controls the cooling water flow of the condenser 2. When the temperature difference between the inlet and outlet of the cooling water in the condenser 2 is reduced, the opening of the first regulating valve 10 is increased to increase the cooling water flow; when the temperature difference between the inlet and outlet of the cooling water in the condenser 2 is increased, the opening is increased, thereby increasing the cooling water flow; when the temperature difference between the inlet and outlet of the cooling water in the condenser 2 is increased, the opening is increased, thereby simulating the user's heating load.
本实施例的不锈钢水泵14的出口经第五调节阀18与中间路换热器15的进口连通,第五调节阀18的进口经第六调节阀19与中间路换热器15的出口连通构成第三旁通管路22,中间路换热器15的出口与经第三调节阀16与蒸发器5的进口连通,第三调节阀16的进口经第四调节阀17与蒸发器5的出口连通构成第二旁通管路21,蒸发器5的出口经膨胀水箱13与不锈钢水泵14的进口连通,从蒸发器5中流出的乙二醇水溶液与来自第二旁通管路21的乙二醇水溶液混合,然后依次流经膨胀水箱13、不锈钢水泵14,通过第五调节阀18、第六调节阀19和中间路换热器15后,经第三调节阀16进入蒸发器5中放热,中间路换热器15将冷凝温度调节系统的热量传递给蒸发温度调节系统,以平衡实验过程中的冷热负荷,降低实验成本。为防止蒸发温度调节系统在低温工况运行时管道结冰,选用乙二醇水溶液作为室外环境模拟系统的换热介质,为实现蒸发温度的灵活调节,由第六调节阀19控制蒸发器5的蒸发温度,降低蒸发温度时,增大第六调节阀19的开度;提高蒸发温度时,则反之,由第三调节阀16和第四调节阀17控制进入蒸发器5的乙二醇水溶液的质量流量,由第四调节阀17控制进入中间路换热器15的乙二醇水溶液的温度,为解决中间路换热器15中介质换热温差大,水侧容易结冰的问题,中间路换热器15中换热介质的相对流向为顺流,换热器中低温乙二醇水溶液与高温热水换热,使换热器壁面温度高于0℃,并设置第三旁通管路22,由第五调节阀18和第六调节阀19调节进入中间路换热器15的乙二醇水溶液的质量流量,当乙二醇水溶液温度过低时,减小第五调节阀18的开度,降低进入中间路换热器15的乙二醇水溶液的质量流量,保证中间路换热器15的水侧出口温度不低于5℃,可有效防止中间路换热器15的水侧结冰,提高系统运行安全性。The outlet of the stainless steel water pump 14 of this embodiment is connected to the inlet of the intermediate heat exchanger 15 through the fifth regulating valve 18, and the inlet of the fifth regulating valve 18 is connected to the outlet of the intermediate heat exchanger 15 through the sixth regulating valve 19 to form a third bypass pipeline 22. The outlet of the intermediate heat exchanger 15 is connected to the inlet of the evaporator 5 through the third regulating valve 16, and the inlet of the third regulating valve 16 is connected to the outlet of the evaporator 5 through the fourth regulating valve 17 to form a second bypass pipeline 21. The outlet of the evaporator 5 is connected to the inlet of the stainless steel water pump 14 through the expansion water tank 13. The ethylene glycol aqueous solution flowing out of the evaporator 5 is mixed with the ethylene glycol aqueous solution from the second bypass pipeline 21, and then flows through the expansion water tank 13, the stainless steel water pump 14 in sequence, passes through the fifth regulating valve 18, the sixth regulating valve 19 and the intermediate heat exchanger 15, and then enters the evaporator 5 through the third regulating valve 16 to release heat. The intermediate heat exchanger 15 transfers the heat of the condensing temperature regulation system to the evaporation temperature regulation system to balance the cold and hot loads during the experiment and reduce the experimental cost. In order to prevent the pipes of the evaporation temperature control system from freezing when operating under low temperature conditions, ethylene glycol aqueous solution is selected as the heat exchange medium of the outdoor environment simulation system. In order to realize flexible adjustment of the evaporation temperature, the evaporation temperature of the evaporator 5 is controlled by the sixth regulating valve 19. When the evaporation temperature is reduced, the opening of the sixth regulating valve 19 is increased; when the evaporation temperature is increased, on the contrary, the mass flow of the ethylene glycol aqueous solution entering the evaporator 5 is controlled by the third regulating valve 16 and the fourth regulating valve 17, and the temperature of the ethylene glycol aqueous solution entering the intermediate heat exchanger 15 is controlled by the fourth regulating valve 17. In order to solve the problem that the medium heat exchange temperature difference in the intermediate heat exchanger 15 is large and the water side is easy to freeze The relative flow direction of the heat exchange medium in the intermediate heat exchanger 15 is downstream. The low-temperature ethylene glycol aqueous solution in the heat exchanger exchanges heat with the high-temperature hot water, so that the wall temperature of the heat exchanger is higher than 0°C. A third bypass pipeline 22 is set, and the mass flow rate of the ethylene glycol aqueous solution entering the intermediate heat exchanger 15 is adjusted by the fifth regulating valve 18 and the sixth regulating valve 19. When the temperature of the ethylene glycol aqueous solution is too low, the opening of the fifth regulating valve 18 is reduced to reduce the mass flow rate of the ethylene glycol aqueous solution entering the intermediate heat exchanger 15, ensuring that the water side outlet temperature of the intermediate heat exchanger 15 is not lower than 5°C, which can effectively prevent the water side of the intermediate heat exchanger 15 from freezing and improve the safety of system operation.
本发明不局限于上述实施方式,任何人应得知在本发明的启示下作出的结构变化,凡是与本发明具有相同或相近的技术方案,均落入本发明的保护范围之内。本发明未详细描述的技术、形状、构造部分均为公知技术。The present invention is not limited to the above-mentioned embodiments. Anyone should be aware that any structural changes made under the enlightenment of the present invention, and any technical solutions that are the same or similar to the present invention, fall within the protection scope of the present invention. The technology, shape, and structural parts not described in detail in the present invention are all well-known technologies.
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