CN104061705B - Two-stage compression air conditioning system and control method thereof - Google Patents
Two-stage compression air conditioning system and control method thereof Download PDFInfo
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- 238000004378 air conditioning Methods 0.000 title claims abstract description 34
- 230000006835 compression Effects 0.000 title claims abstract description 33
- 238000007906 compression Methods 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 19
- 239000003507 refrigerant Substances 0.000 claims abstract description 57
- 238000010257 thawing Methods 0.000 claims abstract description 42
- 238000010438 heat treatment Methods 0.000 claims description 14
- 238000001816 cooling Methods 0.000 claims description 8
- 238000005338 heat storage Methods 0.000 description 20
- 239000011232 storage material Substances 0.000 description 15
- 230000007423 decrease Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 3
- 230000035939 shock Effects 0.000 description 3
- 239000013589 supplement Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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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
- F25B13/00—Compression machines, plants or systems, with reversible cycle
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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
- F25B47/00—Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
- F25B47/02—Defrosting cycles
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Abstract
Description
技术领域technical field
本发明涉及空调技术领域,特别是涉及一种双级压缩空调系统及其控制方法。The invention relates to the technical field of air conditioning, in particular to a two-stage compression air conditioning system and a control method thereof.
背景技术Background technique
目前,带闪蒸器的双级压缩空调系统的中间补气量不可调节,当压缩机采用相同的频率时,系统中其它参数的变化可能导致中间补气量的波动,使压缩机到运行状态偏离最佳效率点,造成压缩机不能在最佳效率点运行。At present, the intermediate air supply volume of the two-stage compression air conditioning system with a flash evaporator cannot be adjusted. When the compressor uses the same frequency, changes in other parameters in the system may cause fluctuations in the intermediate air supply volume, which will make the compressor run from the optimal state. efficiency point, causing the compressor not to operate at the best efficiency point.
另外,双级压缩空调系统常规除霜的方式是制热过程中,达到除霜条件时,压缩机先停机,然后开机转制冷模式,进行除霜。当除霜结束后,再停机,然后开机转回制热模式。这种除霜方式,压缩机经过两次开停,除霜耗时长。且制冷模式下会从室内环境吸收热量,导致除霜过程中室内温度迅速下降,影响用户使用到舒适性。为了解决传统除霜方式存在的上述问题,现有技术提出了一种蓄热除霜方法,该除霜方法采用设置在压缩机壳体上的蓄热器作为除霜工况时的主要低温热源。制冷或制热时,蓄热器吸收压缩机的废热,制热除霜时,四通换向阀不换向,冷媒在室内换热器流出后,经过与电子膨胀阀并联的旁通管路进入到室外换热器进行除霜。虽然该除霜方法可以解决传统除霜方式存在的上述问题,但是,由于该除霜方式是利用压缩机产生的热量来进行蓄热,因此所使用的相变蓄热材料相变温度点必然会较低,蓄热材料吸热和放热速度会较慢,从而使得除霜速度较慢,延长化霜时间,同样影响制热效果和舒适度。尤其对于带除霜功能的双级压缩空调系统,在制热的时候,因为闪蒸器的存在,冷媒在流过闪蒸器的时候必定会被再次过冷,即流入室外换热器的冷媒必定处于相较于单级压缩更低的温度,那么其结霜情况会更严重、更频繁,因此除霜速度更慢。而且,在蓄热器蓄热量不足时进行除霜,会导致大量蒸发不完的制冷剂进入压缩机,从而对压缩机的可靠性造成致命的威胁。In addition, the conventional defrosting method of the two-stage compression air-conditioning system is that during the heating process, when the defrosting condition is reached, the compressor is first stopped, and then turned on to the cooling mode for defrosting. When the defrosting is over, stop the machine, and then turn it back on to the heating mode. In this defrosting method, the compressor starts and stops twice, and the defrosting takes a long time. In addition, in the cooling mode, heat will be absorbed from the indoor environment, causing the indoor temperature to drop rapidly during the defrosting process, affecting the comfort of users. In order to solve the above problems in the traditional defrosting method, the prior art proposes a thermal storage defrosting method, which uses a heat accumulator installed on the compressor housing as the main low-temperature heat source in the defrosting working condition . When cooling or heating, the accumulator absorbs the waste heat of the compressor. When heating and defrosting, the four-way reversing valve does not change direction. After the refrigerant flows out of the indoor heat exchanger, it passes through the bypass pipeline connected in parallel with the electronic expansion valve. into the outdoor heat exchanger for defrosting. Although this defrosting method can solve the above-mentioned problems existing in the traditional defrosting method, since the defrosting method uses the heat generated by the compressor to store heat, the phase change temperature point of the phase change heat storage material used will inevitably be If the temperature is lower, the heat absorption and heat release speed of the heat storage material will be slower, so that the defrosting speed will be slower, and the defrosting time will be prolonged, which will also affect the heating effect and comfort. Especially for the two-stage compression air conditioning system with defrosting function, when heating, due to the existence of the flash evaporator, the refrigerant must be subcooled again when it flows through the flash evaporator, that is, the refrigerant flowing into the outdoor heat exchanger must be at At lower temperatures than with single-stage compression, frosting will be more severe and frequent, and therefore defrost slower. Moreover, defrosting when the heat stored in the heat accumulator is insufficient will cause a large amount of refrigerant that cannot be evaporated to enter the compressor, thereby posing a fatal threat to the reliability of the compressor.
发明内容Contents of the invention
针对上述现有技术现状,本发明所要解决的技术问题在于,提供一种双级压缩空调系统,其中间补气量可调节,并且,除霜速度快,可以避免除霜时蒸发不完的制冷剂进入压缩机对压缩机造成不利影响。Aiming at the current state of the art above, the technical problem to be solved by the present invention is to provide a two-stage compression air-conditioning system, in which the amount of air supply in the middle can be adjusted, and the defrosting speed is fast, which can avoid the refrigerant that cannot be completely evaporated during defrosting. Entering the compressor can adversely affect the compressor.
为了解决上述技术问题,本发明所提供的一种双级压缩空调系统,包括双级压缩机、四通换向阀、室外换热器、第一节流装置、闪蒸器、第二节流装置和室内换热器,所述双级压缩机的排气口和吸气口通过所述四通换向阀与所述室外换热器的第一端接口和所述室内换热器的第一端接口相连通,所述室外换热器的第二端接口通过所述第一节流装置与所述闪蒸器的第一接口相连通,所述闪蒸器的第二接口通过所述第二节流装置与所述室内换热器的第二端接口相连通,所述闪蒸器的第三接口通过补气管路与所述双级压缩机的补气口相连通;In order to solve the above technical problems, a two-stage compression air conditioning system provided by the present invention includes a two-stage compressor, a four-way reversing valve, an outdoor heat exchanger, a first throttling device, a flash evaporator, and a second throttling device and the indoor heat exchanger, the exhaust port and the suction port of the two-stage compressor are connected to the first port of the outdoor heat exchanger and the first port of the indoor heat exchanger through the four-way reversing valve. The second port of the outdoor heat exchanger communicates with the first port of the flash evaporator through the first throttling device, and the second port of the flash evaporator passes through the second section The flow device is connected with the second end interface of the indoor heat exchanger, and the third interface of the flash evaporator is connected with the air supply port of the two-stage compressor through the air supply pipeline;
所述第一节流装置和所述第二节流装置的开度可调节;The openings of the first throttling device and the second throttling device are adjustable;
还包括旁通管路、蓄热器和控制阀,所述旁通管路连接在所述室外换热器的第一端接口与所述双级压缩机的吸气口之间,所述蓄热器具有第一换热管和第二换热管,所述第一换热管串联在所述双级压缩机的排气口与所述室内换热器的第一端接口之间的管路上,所述第二换热管串联在所述旁通管路上,所述控制阀用于选择性地导通或断开所述室外换热器的第一端接口与所述双级压缩机的吸气口之间的管路和所述旁通管路。It also includes a bypass line, a heat accumulator and a control valve, the bypass line is connected between the first port of the outdoor heat exchanger and the suction port of the two-stage compressor, the accumulator The heat exchanger has a first heat exchange tube and a second heat exchange tube, the first heat exchange tube is connected in series between the exhaust port of the two-stage compressor and the first end interface of the indoor heat exchanger On the road, the second heat exchange pipe is connected in series on the bypass pipe, and the control valve is used to selectively connect or disconnect the first port of the outdoor heat exchanger from the two-stage compressor. The pipeline between the suction port and the bypass pipeline.
在其中一个实施例中,所述的双级压缩空调系统还包括第三节流装置,所述第三节流装置串联在所述蓄热器的所述第二换热管入口侧的所述旁通管路上。In one of the embodiments, the two-stage compression air-conditioning system further includes a third throttling device, and the third throttling device is connected in series with the on the bypass line.
在其中一个实施例中,所述第三节流装置为毛细管。In one of the embodiments, the third throttling device is a capillary.
在其中一个实施例中,所述控制阀的通道孔径小于冷媒管的孔径,使经过所述控制阀的冷媒节流后流入所述蓄热器的所述第二换热管。In one of the embodiments, the channel aperture of the control valve is smaller than the aperture of the refrigerant pipe, so that the refrigerant passing through the control valve is throttled and flows into the second heat exchange pipe of the heat accumulator.
在其中一个实施例中,所述旁通管路的一端连接在所述四通换向阀与所述室外换热器的第一端接口之间的管路上,另一端连接在所述四通换向阀与所述双级压缩机的吸气口之间的管路上。In one of the embodiments, one end of the bypass pipeline is connected to the pipeline between the four-way reversing valve and the first port of the outdoor heat exchanger, and the other end is connected to the four-way reversing valve. On the pipeline between the reversing valve and the suction port of the two-stage compressor.
在其中一个实施例中,所述旁通管路的两端均连接在所述四通换向阀与所述双级压缩机的吸气口之间的管路上。In one embodiment, both ends of the bypass pipeline are connected to the pipeline between the four-way reversing valve and the suction port of the two-stage compressor.
在其中一个实施例中,所述控制阀为三通阀。In one of the embodiments, the control valve is a three-way valve.
在其中一个实施例中,所述第一节流装置和所述第二节流装置均为电子膨胀阀。In one of the embodiments, both the first throttling device and the second throttling device are electronic expansion valves.
在其中一个实施例中,所述补气管路上设置有补气阀。In one of the embodiments, an air supply valve is arranged on the air supply pipeline.
本发明所提供的一种双级压缩空调系统的控制方法,包括:A control method for a two-stage compression air-conditioning system provided by the present invention includes:
制冷或制热运行时,所述控制阀导通所述室外换热器的第一端接口与所述双级压缩机的吸气口之间的管路、断开所述旁通管路,通过调节所述第一节流装置和/或所述第二节流装置的开度大小调节经过所述补气管路的制冷剂的流量大小;During cooling or heating operation, the control valve connects the pipeline between the first end interface of the outdoor heat exchanger and the suction port of the two-stage compressor, disconnects the bypass pipeline, adjusting the flow rate of the refrigerant passing through the air supply pipeline by adjusting the opening of the first throttling device and/or the second throttling device;
除霜运行时,所述控制阀断开所述室外换热器的第一端接口与所述双级压缩机的吸气口之间的管路、导通所述旁通管路。During the defrosting operation, the control valve disconnects the pipeline between the first end interface of the outdoor heat exchanger and the suction port of the two-stage compressor, and connects the bypass pipeline.
在其中一个实施例中,除霜运行时,所述补气管路断开。In one of the embodiments, when the defrosting is running, the air supply line is disconnected.
与现有技术相比,本发明的双级压缩空调系统及其控制方法,由于第一节流装置和第二节流装置的开度可调节,通过调节第一节流装置和/或第二节流装置的开度大小即可调节经过补气管路的制冷剂的流量大小,从而可以有效到调节中间补气段的进气量,使系统运行在最佳效率点附近,提高了系统的运行效率;而且,该双级压缩空调系统利用压缩机直接排出的高温制冷剂进行蓄热,因此可以采用相变温度点较高的相变蓄热材料,这样,在除霜时,相变蓄热材料与制冷剂的温差加大,相变蓄热材料的放热速度快,相应除霜速度也会加快,保证了用户使用的舒适性。而且,除霜时蓄热器蓄热量充足,避免了蒸发不完的制冷剂进入压缩机造成液击,从而对压缩机的可靠性造成致命的威胁。Compared with the prior art, the two-stage compression air-conditioning system and its control method of the present invention, since the opening of the first throttling device and the second throttling device can be adjusted, by adjusting the first throttling device and/or the second throttling device The opening of the throttling device can adjust the flow rate of the refrigerant passing through the air supply pipeline, so that it can effectively adjust the intake air volume in the middle air supply section, so that the system can run near the best efficiency point and improve the operation of the system. efficiency; moreover, the two-stage compression air-conditioning system uses the high-temperature refrigerant directly discharged from the compressor to store heat, so a phase change heat storage material with a higher phase change temperature can be used, so that during defrosting, the phase change heat storage The temperature difference between the material and the refrigerant increases, the heat release speed of the phase change heat storage material is fast, and the corresponding defrosting speed will also be accelerated, ensuring the comfort of the user. Moreover, the accumulator has sufficient heat storage capacity during defrosting, which prevents the refrigerant from evaporating into the compressor and causing liquid shock, which poses a fatal threat to the reliability of the compressor.
本发明附加技术特征所具有的有益效果将在本说明书具体实施方式部分进行说明。The beneficial effects of the additional technical features of the present invention will be described in the specific embodiments of this specification.
附图说明Description of drawings
图1为本发明其中一个实施例中的双级压缩空调系统的系统图;Fig. 1 is a system diagram of a two-stage compression air-conditioning system in one of the embodiments of the present invention;
图2为图1中的双级压缩空调系统制冷时的流程示意图;Fig. 2 is a schematic flow chart of the two-stage compression air-conditioning system in Fig. 1 during refrigeration;
图3为图1中的双级压缩空调系统制热时的流程示意图;Fig. 3 is a schematic flow chart of the two-stage compression air-conditioning system in Fig. 1 during heating;
图4为图1中的双级压缩空调系统除霜时的流程示意图。FIG. 4 is a schematic flow chart of the two-stage compression air-conditioning system in FIG. 1 during defrosting.
附图标记说明:1、双级压缩机;2、室内换热器;3、第二节流装置;4、闪蒸器;5、第一节流装置;6、室外换热器;7、三通阀;8、四通换向阀;9、补气阀;10、第三节流装置;11、蓄热器;11a、第一换热管;11b、第二换热管;12、补气管路;13、旁通管路。Explanation of reference signs: 1. Two-stage compressor; 2. Indoor heat exchanger; 3. Second throttling device; 4. Flash evaporator; 5. First throttling device; 6. Outdoor heat exchanger; 7. Three Through valve; 8. Four-way reversing valve; 9. Air supply valve; 10. Third throttling device; 11. Regenerator; 11a. First heat exchange tube; 11b. Second heat exchange tube; 12. Supplement 13. Bypass pipeline.
具体实施方式detailed description
下面参考附图并结合实施例对本发明进行详细说明。需要说明的是,在不冲突的情况下,以下各实施例及实施例中的特征可以相互组合。The present invention will be described in detail below with reference to the accompanying drawings and examples. It should be noted that, in the case of no conflict, the following embodiments and features in the embodiments can be combined with each other.
如图1所示,本发明其中一个实施例中的双级压缩空调系统包括双级压缩机1、四通换向阀8、室外换热器6、第一节流装置5、闪蒸器4、第二节流装置3、室内换热器2、旁通管路13、蓄热器11和控制阀。As shown in Figure 1, the two-stage compression air conditioning system in one of the embodiments of the present invention includes a two-stage compressor 1, a four-way reversing valve 8, an outdoor heat exchanger 6, a first throttling device 5, a flash evaporator 4, The second throttling device 3, the indoor heat exchanger 2, the bypass pipeline 13, the heat accumulator 11 and the control valve.
其中,所述双级压缩机1的排气口和吸气口通过所述四通换向阀8与所述室外换热器6的第一端接口6a和所述室内换热器2的第一端接口2a相连通,所述室外换热器6的第二端接口6b通过所述第一节流装置5与所述闪蒸器4的第一接口相连通,所述闪蒸器4的第二接口通过所述第二节流装置3与所述室内换热器2的第二端接口2b相连通,所述闪蒸器4的第三接口通过补气管路12与所述双级压缩机1的补气口相连通。所述第一节流装置5和所述第二节流装置3的开度可调节,这样,通过调节第一节流装置5和/或第二节流装置3的开度大小即可调节经过补气管路12的制冷剂的流量大小,从而可以有效到调节中间补气段的进气量,使系统运行在最佳效率点附近,提高了系统的运行效率。Wherein, the exhaust port and the suction port of the two-stage compressor 1 are connected to the first port 6a of the outdoor heat exchanger 6 and the first port of the indoor heat exchanger 2 through the four-way reversing valve 8 . One end interface 2a is connected, the second end interface 6b of the outdoor heat exchanger 6 is communicated with the first interface of the flash evaporator 4 through the first throttling device 5, and the second end interface 6b of the flash evaporator 4 The interface communicates with the second end interface 2b of the indoor heat exchanger 2 through the second throttling device 3, and the third interface of the flash evaporator 4 communicates with the two-stage compressor 1 through the air supply pipeline 12. The gas supply port is connected. The opening of the first throttling device 5 and the second throttling device 3 can be adjusted, so that the passage can be adjusted by adjusting the opening of the first throttling device 5 and/or the second throttling device 3 The flow rate of the refrigerant in the air supply pipeline 12 can effectively adjust the intake air volume in the middle air supply section, so that the system can operate near the optimum efficiency point, and the operating efficiency of the system can be improved.
所述旁通管路13连接在所述室外换热器6的第一端接口6a与所述双级压缩机1的吸气口之间,本实施例中,所述旁通管路13的一端连接在所述四通换向阀8与所述室外换热器6的第一端接口之间的管路上,另一端连接在所述四通换向阀8与所述双级压缩机1的吸气口之间的管路上。当然,所述旁通管路13还可以两端均连接在所述四通换向阀8与所述双级压缩机1的吸气口之间的管路上。The bypass pipeline 13 is connected between the first end interface 6a of the outdoor heat exchanger 6 and the suction port of the two-stage compressor 1. In this embodiment, the bypass pipeline 13 One end is connected to the pipeline between the four-way reversing valve 8 and the first port of the outdoor heat exchanger 6, and the other end is connected to the four-way reversing valve 8 and the two-stage compressor 1 on the pipeline between the suction ports. Of course, both ends of the bypass pipeline 13 can also be connected to the pipeline between the four-way reversing valve 8 and the suction port of the two-stage compressor 1 .
所述蓄热器11具有第一换热管11a和第二换热管11b,所述第一换热管11a串联在所述双级压缩机1的排气口与所述四通换向阀8之间的管路上,第一换热管11a也可以连接在四通换向阀8与所述室内换热器2的第一端接口之间的管路上;所述第二换热管11b串联在所述旁通管路13上。The heat accumulator 11 has a first heat exchange pipe 11a and a second heat exchange pipe 11b, and the first heat exchange pipe 11a is connected in series between the exhaust port of the two-stage compressor 1 and the four-way reversing valve. 8, the first heat exchange tube 11a can also be connected to the pipeline between the four-way reversing valve 8 and the first end interface of the indoor heat exchanger 2; the second heat exchange tube 11b connected in series to the bypass line 13.
所述控制阀用于选择性地导通或断开所述室外换热器6的第一端接口与所述双级压缩机1的吸气口之间的管路和所述旁通管路13。优选地,所述控制阀为三通阀7,三通阀7也可以采用两个二通阀代替。The control valve is used to selectively connect or disconnect the pipeline between the first port of the outdoor heat exchanger 6 and the suction port of the two-stage compressor 1 and the bypass pipeline 13. Preferably, the control valve is a three-way valve 7, and the three-way valve 7 can also be replaced by two two-way valves.
本实施例的双级压缩空调系统利用压缩机直接排出的高温制冷剂进行蓄热,因此可以采用相变温度点较高的相变蓄热材料,这样,在除霜时,相变蓄热材料与制冷剂的温差加大,相变蓄热材料的放热速度快,相应除霜速度也会加快,保证了用户使用的舒适性。而且,除霜时蓄热器11蓄热量充足,避免了蒸发不完的制冷剂进入压缩机造成液击,从而对压缩机的可靠性造成致命的威胁。The two-stage compression air-conditioning system of this embodiment uses the high-temperature refrigerant directly discharged from the compressor to store heat, so a phase change heat storage material with a higher phase change temperature can be used, so that when defrosting, the phase change heat storage material As the temperature difference with the refrigerant increases, the heat release speed of the phase change heat storage material is fast, and the corresponding defrosting speed will also be accelerated, ensuring the comfort of the user. Moreover, the heat accumulator 11 has sufficient heat storage during defrosting, which prevents the incompletely evaporated refrigerant from entering the compressor and causing liquid hammer, thereby posing a fatal threat to the reliability of the compressor.
优选地,还包括第三节流装置10,所述第三节流装置10串联在所述第二换热管11b入口侧的所述旁通管路13上。进一步优选地,所述第三节流装置10为毛细管。这样,室外换热器6出口的冷媒通过毛细管节流后,再进入蓄热器11吸热蒸发,有利于液体冷媒完全蒸发,避免了蒸发不完的制冷剂进入双级压缩机1造成液击。当然,毛细管也可以用通道孔径小于冷媒管孔径的三通阀7代替,这样三通阀7也可以起到节流作用。Preferably, a third throttling device 10 is further included, and the third throttling device 10 is connected in series on the bypass line 13 on the inlet side of the second heat exchange tube 11b. Further preferably, the third throttling device 10 is a capillary. In this way, the refrigerant at the outlet of the outdoor heat exchanger 6 is throttled by the capillary tube, and then enters the accumulator 11 to absorb heat and evaporate, which is conducive to the complete evaporation of the liquid refrigerant, and avoids the liquid shock caused by the endlessly evaporated refrigerant entering the two-stage compressor 1 . Of course, the capillary tube can also be replaced by a three-way valve 7 with a channel aperture smaller than that of the refrigerant pipe, so that the three-way valve 7 can also play a throttling role.
优选地,所述补气管路12上设置有补气阀9,通过补气阀9控制补气管路12的导通和断开。Preferably, the air supply line 12 is provided with an air supply valve 9 , and the conduction and disconnection of the air supply line 12 are controlled by the air supply valve 9 .
本发明还提供一种双级压缩空调系统的控制方法,包括以下步骤:The present invention also provides a control method for a two-stage compression air-conditioning system, comprising the following steps:
步骤1、制冷或制热运行时,所述三通阀7导通所述室外换热器6的第一端接口与所述双级压缩机1的吸气口之间的管路、断开所述旁通管路13,所述补气阀9打开,通过调节所述第一节流装置5和/或所述第二节流装置3的开度大小调节经过所述补气管路12的制冷剂的流量大小。具体过程如下:Step 1. During cooling or heating operation, the three-way valve 7 connects the pipeline between the first end interface of the outdoor heat exchanger 6 and the suction port of the two-stage compressor 1, disconnects In the bypass pipeline 13, the supplementary air valve 9 is opened, and the gas passing through the supplementary supplementary pipeline 12 is adjusted by adjusting the opening of the first throttling device 5 and/or the second throttling device 3 . The flow rate of refrigerant. The specific process is as follows:
系统制冷运行时,见图2,由双级压缩机1排气口出来的高温高压气体经过蓄热器11的第一换热管11a与相变蓄热材料进行热交换,相变蓄热材料吸热并发生相变,将热量储存起来,然后冷媒经四通换向阀8进入室外换热器6,并与室外环境换热,释放热量,冷媒先流经第一节流装置5,再进入闪蒸器4汽化,闪蒸器4分离出来的液态冷媒经第二节流装置3节流后进入室内换热器2,与室内环境进行换热,吸收室内热量环境热量,最后经过四通换向阀8进入双级压缩机1吸气口,完成一次制冷循环;闪蒸器4分离出来的气态冷媒经补气阀9进入双级压缩机1的补气口。当需要增大补气量时,开大第一节流装置5的开度,关小或维持第二节流装置3的开度,这样进入闪蒸器4的冷媒量增大,流出的冷媒量减小或不变,则中间补气量增大;或者,关小第一节流装置5的开度,同时更多地关小第二节流装置3的开度,这时虽然进入闪蒸器4的冷媒减少,但流出闪蒸器4的冷媒量减小的幅度更大,中间补气量增大。反之,当需要减小补气量时,关小第一节流装置5的开度,关大或维持第二节流装置3的开度,这样进入闪蒸器4的冷媒量减小,流出的冷媒量增加或不变,则中间补气量减小;或者,增大第一节流装置5的开度,同时更多地增大第二节流装置3的开度,这时虽然进入闪蒸器4的冷媒增加,但流出闪蒸器4的冷媒量增加的幅度更大,中间补气量减小。When the system is in cooling operation, as shown in Figure 2, the high-temperature and high-pressure gas from the exhaust port of the two-stage compressor 1 passes through the first heat exchange tube 11a of the heat accumulator 11 to exchange heat with the phase-change heat storage material, and the phase-change heat storage material It absorbs heat and undergoes a phase change to store the heat, then the refrigerant enters the outdoor heat exchanger 6 through the four-way reversing valve 8, and exchanges heat with the outdoor environment to release heat. The refrigerant first flows through the first throttling device 5, and then Enter the flash evaporator 4 to vaporize, the liquid refrigerant separated from the flash evaporator 4 enters the indoor heat exchanger 2 after being throttled by the second throttling device 3, exchanges heat with the indoor environment, absorbs indoor heat and environmental heat, and finally passes through the four-way reversing The valve 8 enters the suction port of the two-stage compressor 1 to complete a refrigeration cycle; the gaseous refrigerant separated from the flash evaporator 4 enters the air supply port of the two-stage compressor 1 through the air supply valve 9 . When it is necessary to increase the amount of supplementary air, open the opening degree of the first throttling device 5, close or maintain the opening degree of the second throttling device 3, so that the amount of refrigerant entering the flash evaporator 4 increases, and the amount of refrigerant flowing out decreases. If it is small or unchanged, the amount of supplementary air in the middle will increase; or, turn down the opening degree of the first throttling device 5 and at the same time turn down the opening degree of the second throttling device 3 more. The refrigerant decreases, but the amount of refrigerant flowing out of the flash evaporator 4 decreases even more, and the amount of air supplemented in the middle increases. Conversely, when it is necessary to reduce the amount of supplementary air, close the opening of the first throttling device 5, and close or maintain the opening of the second throttling device 3, so that the amount of refrigerant entering the flash evaporator 4 is reduced, and the refrigerant flowing out If the air volume increases or remains unchanged, the amount of intermediate supplementary air will decrease; or, increase the opening degree of the first throttling device 5 and at the same time increase the opening degree of the second throttling device 3 more, even though it enters the flasher 4 The amount of refrigerant increased, but the amount of refrigerant flowing out of the flash evaporator 4 increased even more, and the amount of air replenishment in the middle decreased.
系统制热运行时,见图3,由双级压缩机1排气口出来的高温高压气体经过蓄热器11的第一换热管11a与相变蓄热材料进行热交换,相变蓄热材料吸热并发生相变,将热量储存起来,然后冷媒经四通换向阀8进入室内换热器2,在室内换热器2冷凝放热,然后再经第二节流装置3节流后进入闪蒸器4进行气液分离,闪蒸器4分离出来的液态冷媒经第一节流装置5节流后进入室外换热器6,在室外换热器6进行蒸发,吸收热量,最后经过三通阀7和四通换向阀8进入双级压缩机1吸气口,完成一次制热循环;闪蒸器4分离出来的气态冷媒经补气阀9进入双级压缩机1的补气口。当需要增大补气量时,开大第二节流装置3的开度,关小或维持第一节流装置5的开度,这样进入闪蒸器4的冷媒量增大,流出的冷媒量减小或不变,则中间补气量增大;或者,关小第二节流装置3的开度,同时更多地关小第一节流装置5的开度,这时虽然进入闪蒸器4的冷媒减少,但流出闪蒸器4的冷媒量减小的幅度更大,中间补气量增大。反之,当需要减小补气量时,关小第二节流装置3的开度,关大或维持第一节流装置5的开度,这样进入闪蒸器4的冷媒量减小,流出的冷媒量增加或不变,则中间补气量减小;或者,增大第二节流装置3的开度,同时更多地增大第一节流装置5的开度,这时虽然进入闪蒸器4的冷媒增加,但流出闪蒸器4的冷媒量增加的幅度更大,中间补气量减小。When the system is in heating operation, as shown in Figure 3, the high-temperature and high-pressure gas from the exhaust port of the two-stage compressor 1 passes through the first heat exchange tube 11a of the heat accumulator 11 to exchange heat with the phase-change heat storage material, and the phase-change heat storage The material absorbs heat and undergoes a phase change to store the heat, then the refrigerant enters the indoor heat exchanger 2 through the four-way reversing valve 8, condenses and releases heat in the indoor heat exchanger 2, and then throttles through the second throttling device 3 After entering the flash evaporator 4 for gas-liquid separation, the liquid refrigerant separated from the flash evaporator 4 is throttled by the first throttling device 5 and then enters the outdoor heat exchanger 6, where it evaporates and absorbs heat, and finally passes through three The one-way valve 7 and the four-way reversing valve 8 enter the suction port of the two-stage compressor 1 to complete a heating cycle; the gaseous refrigerant separated from the flash evaporator 4 enters the air supply port of the two-stage compressor 1 through the air supply valve 9 . When it is necessary to increase the amount of supplementary air, open the opening degree of the second throttling device 3, close or maintain the opening degree of the first throttling device 5, so that the amount of refrigerant entering the flash evaporator 4 increases, and the amount of refrigerant flowing out decreases. If it is small or unchanged, the amount of air supply in the middle will increase; or, turn down the opening degree of the second throttling device 3 and at the same time turn down the opening degree of the first throttling device 5 more. The refrigerant decreases, but the amount of refrigerant flowing out of the flash evaporator 4 decreases even more, and the amount of air supplemented in the middle increases. Conversely, when it is necessary to reduce the amount of supplementary air, close the opening of the second throttling device 3 small, and close or maintain the opening of the first throttling device 5, so that the amount of refrigerant entering the flash evaporator 4 is reduced, and the refrigerant flowing out If the air volume increases or does not change, the amount of air supply in the middle will decrease; or, increase the opening of the second throttling device 3 and at the same time increase the opening of the first throttling device 5 more, even though it enters the flasher 4 The amount of refrigerant increased, but the amount of refrigerant flowing out of the flash evaporator 4 increased even more, and the amount of air replenishment in the middle decreased.
由此可见,由于第一节流装置5和第二节流装置3的开度可调节,通过调节第一节流装置5和/或第二节流装置3的开度大小即可调节经过补气管路12的制冷剂的流量大小,从而可以实现中间补气量的控制,使系统最佳效率点附近运行。It can be seen that, since the openings of the first throttling device 5 and the second throttling device 3 can be adjusted, by adjusting the opening degree of the first throttling device 5 and/or the second throttling device 3, it is possible to adjust the The flow rate of the refrigerant in the air pipeline 12 can be controlled so as to realize the control of the amount of air supply in the middle, so that the system can operate near the best efficiency point.
步骤2、除霜运行时,所述三通阀7断开所述室外换热器6的第一端接口与所述双级压缩机1的吸气口之间的管路、导通所述旁通管路13,所述补气阀9关闭。具体过程如下:Step 2. During defrosting operation, the three-way valve 7 disconnects the pipeline between the first end interface of the outdoor heat exchanger 6 and the suction port of the two-stage compressor 1, and conducts the Bypass pipeline 13, the gas supplement valve 9 is closed. The specific process is as follows:
当系统由制热运行进入除霜时,见图4,双级压缩机1排气口排出的高温冷媒流经蓄热器11的第一换热管11a与相变蓄热材料进行热交换,相变蓄热材料吸热并发生相变,将热量储存起来,然后冷媒经四通换向阀8进入室内换热器2,为了减小热量损失,此时室内风机为关闭或低风挡状态。流经室内换热器2后冷媒只有少量的热损失,然后流经第二节流装置3、闪蒸器4、第一节流装置5,为保证在流经这三个元件的时候冷媒的热损失尽量减小,第二节流装置3和第一节流装置5的开度开到最大,关闭补气阀9。然后高温冷媒进入室外换热器6进行除霜;在室外换热器6内冷凝换热后,再通过三通阀7换向进入蓄热器11的第二换热管11b,吸收蓄热器11内积蓄的热量,进行蒸发,然后进入双级压缩机1吸气口,完成除霜循环。When the system enters defrosting from heating operation, as shown in Figure 4, the high-temperature refrigerant discharged from the exhaust port of the two-stage compressor 1 flows through the first heat exchange tube 11a of the heat accumulator 11 to exchange heat with the phase change heat storage material, The phase change heat storage material absorbs heat and undergoes phase change to store the heat, and then the refrigerant enters the indoor heat exchanger 2 through the four-way reversing valve 8. In order to reduce heat loss, the indoor fan is turned off or in a low windshield state. After flowing through the indoor heat exchanger 2, the refrigerant has only a small amount of heat loss, and then flows through the second throttling device 3, the flash evaporator 4, and the first throttling device 5. The loss is minimized, the openings of the second throttling device 3 and the first throttling device 5 are opened to the maximum, and the air supplement valve 9 is closed. Then the high-temperature refrigerant enters the outdoor heat exchanger 6 for defrosting; after condensing and exchanging heat in the outdoor heat exchanger 6, it is then reversed through the three-way valve 7 and enters the second heat exchange tube 11b of the heat accumulator 11 to absorb the heat of the heat accumulator. The heat accumulated in 11 is evaporated, and then enters the suction port of the two-stage compressor 1 to complete the defrosting cycle.
由此可见,本发明实施例的双级压缩空调系统,利用压缩机直接排出的高温制冷剂进行蓄热,因此可以采用相变温度点较高的相变蓄热材料,这样,在除霜时,相变蓄热材料与制冷剂的温差加大,相变蓄热材料的放热速度快,相应除霜速度也会加快,保证了用户使用的舒适性。而且,除霜时蓄热器蓄热量充足,避免了蒸发不完的制冷剂进入压缩机造成液击,从而对压缩机的可靠性造成致命的威胁。It can be seen that the two-stage compression air-conditioning system of the embodiment of the present invention uses the high-temperature refrigerant directly discharged from the compressor to store heat, so a phase-change heat storage material with a higher phase-change temperature can be used. In this way, when defrosting , The temperature difference between the phase change heat storage material and the refrigerant increases, the heat release speed of the phase change heat storage material is fast, and the corresponding defrosting speed will also be accelerated, ensuring the comfort of the user. Moreover, the accumulator has sufficient heat storage capacity during defrosting, which prevents the refrigerant from evaporating into the compressor and causing liquid shock, which poses a fatal threat to the reliability of the compressor.
以上所述实施例仅表达了本发明的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对本发明专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围。The above-mentioned embodiments only express several implementation modes of the present invention, and the description thereof is relatively specific and detailed, but should not be construed as limiting the patent scope of the present invention. It should be pointed out that those skilled in the art can make several modifications and improvements without departing from the concept of the present invention, and these all belong to the protection scope of the present invention.
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