CN204806586U - Evaporation cooling formula cooling water set - Google Patents
Evaporation cooling formula cooling water set Download PDFInfo
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- CN204806586U CN204806586U CN201520481732.7U CN201520481732U CN204806586U CN 204806586 U CN204806586 U CN 204806586U CN 201520481732 U CN201520481732 U CN 201520481732U CN 204806586 U CN204806586 U CN 204806586U
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Abstract
本实用新型公开了一种蒸发冷却式冷水机组,包括压缩机、冷凝器、节流装置、蒸发器,所述蒸发器设有冷冻液进口端和冷冻液出口端;为了节省处理高温回水时的能耗,提高整机能效比,该蒸发冷却式冷水机组还包括蒸发式冷却装置;所述蒸发式冷却装置设有冷冻液进口和冷冻液出口,所述冷冻液出口与所述冷冻液进口端管道相通。蒸发冷却式冷水机组通过在传统的冷水机组上增设蒸发式冷却装置,使待降温冷冻液先经过蒸发式冷却装置作前置降温后再进入到蒸发器中作二次降温,相对于不设有蒸发式冷却装置只能利用蒸发器作一次降温的传统冷水机组,能够有助于节省处理高温回水时的能耗,大大地提高了整机的能效比。
The utility model discloses an evaporative cooling chiller, which comprises a compressor, a condenser, a throttling device, and an evaporator. The evaporator is provided with a refrigerating liquid inlet and a refrigerating liquid outlet; The energy consumption of the whole machine improves the energy efficiency ratio of the whole machine. The evaporative cooling chiller also includes an evaporative cooling device; the evaporative cooling device is provided with a cooling liquid inlet and a cooling liquid outlet, and the cooling liquid outlet and the cooling liquid inlet The end pipes are connected. The evaporative cooling chiller adds an evaporative cooling device to the traditional chiller, so that the frozen liquid to be cooled first passes through the evaporative cooling device for pre-cooling and then enters the evaporator for secondary cooling. The evaporative cooling device can only use the evaporator for one-time cooling of the traditional chiller, which can help save energy consumption when processing high-temperature return water, and greatly improve the energy efficiency ratio of the whole machine.
Description
技术领域technical field
本实用新型涉及冷水机组技术领域,尤其涉及一种蒸发冷却式冷水机组。The utility model relates to the technical field of chillers, in particular to an evaporative cooling chiller.
背景技术Background technique
在空调应用中,通常是采用将回水直接送入冷水机组的蒸发器中进行冷却,但当回水温度较高而需求供水温度较低时,采用该方式时,蒸发器则需提供低于出水温度的蒸发温度,导致传热温差大,不可逆损失大,即需要冷水机组耗费大量的能耗去处理高温的回水,使得整机能效比低、耗能大。In air conditioning applications, the return water is usually sent directly to the evaporator of the chiller for cooling, but when the return water temperature is high and the required supply water temperature is low, when this method is used, the evaporator needs to provide less than The evaporation temperature of the outlet water temperature leads to a large heat transfer temperature difference and a large irreversible loss, that is, the chiller needs to consume a lot of energy to process the high-temperature return water, which makes the energy efficiency ratio of the whole machine low and consumes a lot of energy.
实用新型内容Utility model content
为了克服现有技术的不足,本实用新型的目的在于提供一种蒸发冷却式冷水机组,其可以节省处理高温回水时的能耗,提高整机的能效比。In order to overcome the deficiencies of the prior art, the purpose of this utility model is to provide an evaporative cooling chiller, which can save energy consumption when processing high-temperature return water, and improve the energy efficiency ratio of the whole machine.
为解决上述问题,本实用新型所采用的技术方案如下:In order to solve the above problems, the technical scheme adopted in the utility model is as follows:
一种蒸发冷却式冷水机组,包括压缩机、冷凝器、节流装置、蒸发器,所述蒸发器设有冷冻液进口端和冷冻液出口端;为了节省处理高温回水时的能耗,提高整机能效比,该蒸发冷却式冷水机组还包括蒸发式冷却装置;所述蒸发式冷却装置设有冷冻液进口和冷冻液出口,所述冷冻液出口与所述冷冻液进口端管道相通。An evaporative cooling chiller, comprising a compressor, a condenser, a throttling device, and an evaporator, the evaporator is provided with a refrigerant inlet port and a refrigerant outlet port; in order to save energy consumption when processing high-temperature return water, improve The overall energy efficiency ratio, the evaporative cooling chiller also includes an evaporative cooling device; the evaporative cooling device is provided with a cooling liquid inlet and a cooling liquid outlet, and the cooling liquid outlet is connected to the cooling liquid inlet pipe.
进一步地,所述压缩机的排气口管道连接冷凝器的气体管,所述冷凝器的液体管通过所述节流装置连接所述蒸发器的液体管;所述蒸发器的气体管管道连接所述压缩机的吸气口。Further, the exhaust pipe of the compressor is connected to the gas pipe of the condenser, and the liquid pipe of the condenser is connected to the liquid pipe of the evaporator through the throttling device; the gas pipe of the evaporator is connected to The suction port of the compressor.
作为本实用新型蒸发冷却式冷水机组的改进方案,所述蒸发式冷却装置包括N个蒸发式冷却单元,每个所述蒸发式冷却单元均设有进液口和出液口;所述N个蒸发式冷却单元的进、出液口通过管道依次串连,并且所述冷冻液进口为第一个蒸发式冷却单元的进液口,所述冷冻液出口为第N个蒸发式冷却单元的出液口;所述N为正整数。As an improved scheme of the evaporative cooling water chiller of the utility model, the evaporative cooling device includes N evaporative cooling units, and each of the evaporative cooling units is provided with a liquid inlet and a liquid outlet; the N The liquid inlet and outlet ports of the evaporative cooling units are connected in series through pipelines, and the refrigerant inlet is the liquid inlet of the first evaporative cooling unit, and the refrigerant outlet is the outlet of the Nth evaporative cooling unit. liquid port; said N is a positive integer.
优选地,进入所述进液口的冷冻液为空调系统的回水、空调系统的供水、以及回水经过冷却后中间过程的空调水三者中的一种或两种以上。Preferably, the refrigerant entering the liquid inlet is one or more of the return water of the air conditioning system, the supply water of the air conditioning system, and the air conditioning water in the intermediate process after the return water is cooled.
优选地,所述蒸发式冷却单元还包括壳体,设于壳体顶部出风口上的抽风机,设于壳体侧面进风口中的第一换热器,设于壳体内的冷却液集液盘和冷却液循环泵,以及设于壳体内且位于连通所述进风口与抽风机的风道之中的冷却液喷淋器和第二换热器;所述冷却液喷淋器和冷却液集液盘分别位于第二换热器上方和下方;所述第一换热器为气-液换热器;所述第二换热器至少设有冷冻液管道;进液口、第一换热器进液端、第一换热器出液端、冷冻液管道入口、冷冻液管道出口、出液口依次管道相通;所述冷却液循环泵入口管道连通所述冷却液集液盘,冷却液循环泵出口管道连通所述冷却液喷淋器。Preferably, the evaporative cooling unit further includes a casing, an exhaust fan arranged on the air outlet on the top of the casing, a first heat exchanger arranged in the air inlet on the side of the casing, and a cooling liquid collecting liquid arranged in the casing The pan and the cooling liquid circulation pump, and the cooling liquid sprayer and the second heat exchanger which are arranged in the casing and are located in the air passage connecting the air inlet and the exhaust fan; the cooling liquid sprayer and the cooling liquid The liquid collecting tray is respectively located above and below the second heat exchanger; the first heat exchanger is a gas-liquid heat exchanger; the second heat exchanger is at least provided with a cooling liquid pipeline; the liquid inlet, the first heat exchanger The liquid inlet end of the heat exchanger, the liquid outlet end of the first heat exchanger, the inlet of the cooling liquid pipeline, the outlet of the cooling liquid pipeline, and the liquid outlet are sequentially connected by pipelines; The outlet pipe of the liquid circulation pump is connected to the coolant sprayer.
更优选地,所述第一换热器的数量为一个或多个,所述进风口与所述第一换热器一一对应,对应的第一换热器设置在对应进风口之中;所述第二换热器的数量为一个或多个。More preferably, the number of the first heat exchangers is one or more, the air inlets correspond to the first heat exchangers one by one, and the corresponding first heat exchangers are arranged in the corresponding air inlets; The number of the second heat exchanger is one or more.
更优选地,所述第一换热器为翅片式换热器或微通道式换热器中的任何一种;所述第二换热器为微通道式换热器或蛇形管式换热器或板片式换热器或板管式换热器中的任何一种。More preferably, the first heat exchanger is any one of a finned heat exchanger or a micro-channel heat exchanger; the second heat exchanger is a micro-channel heat exchanger or a coiled tube Any of the heat exchangers or plate-fin heat exchangers or plate-and-tube heat exchangers.
进一步地,所述冷凝器为蒸发式冷凝器或水冷式冷凝器或风冷式冷凝器中的任何一种。Further, the condenser is any one of evaporative condenser, water-cooled condenser or air-cooled condenser.
更进一步地,所述冷凝器为蒸发式冷凝器,所述N为2以上的正整数,所述蒸发式冷却单元的出风口部分或全部连通所述蒸发式冷凝器的进风口。Furthermore, the condenser is an evaporative condenser, the N is a positive integer greater than 2, and part or all of the air outlet of the evaporative cooling unit is connected to the air inlet of the evaporative condenser.
或者,所述冷凝器为风冷式冷凝器,所述N为2以上的正整数,所述蒸发式冷却单元的出风口部分或全部连通所述风冷式冷凝器的进风口。Alternatively, the condenser is an air-cooled condenser, the N is a positive integer greater than 2, and part or all of the air outlet of the evaporative cooling unit is connected to the air inlet of the air-cooled condenser.
相比现有技术,本实用新型的有益效果在于:Compared with the prior art, the beneficial effects of the utility model are:
本实用新型的蒸发冷却式冷水机组通过在传统的冷水机组上增设蒸发式冷却装置,使待降温冷冻液先经过蒸发式冷却装置作前置降温后再进入到蒸发器中作二次降温,相对于不设有蒸发式冷却装置只能利用蒸发器作一次降温的传统冷水机组,能够有助于节省处理高温回水时的能耗,大大地提高了整机的能效比。The evaporative cooling chiller of the utility model adds an evaporative cooling device to the traditional chiller, so that the frozen liquid to be cooled first passes through the evaporative cooling device for pre-cooling and then enters the evaporator for secondary cooling. For the traditional chiller that does not have an evaporative cooling device and can only use the evaporator for one-time cooling, it can help save energy consumption when processing high-temperature return water, and greatly improve the energy efficiency ratio of the whole machine.
上述说明仅是本实用新型技术方案的概述,为了能够更清楚了解本实用新型的技术手段,而可依照说明书的内容予以实施,并且为了让本实用新型的上述和其他目的、特征和优点能够更明显易懂,以下特举较佳实施例,并配合附图,详细说明如下。The above description is only an overview of the technical solutions of the present utility model. In order to better understand the technical means of the present utility model, it can be implemented according to the contents of the description, and in order to make the above-mentioned and other purposes, features and advantages of the present utility model better It is obvious and easy to understand. The preferred embodiments are specifically cited below, together with the accompanying drawings, and detailed descriptions are as follows.
附图说明Description of drawings
图1为本实用新型的蒸发冷却式冷水机组第一种较优选实施例的结构示意图;Fig. 1 is the structural representation of the first preferred embodiment of the evaporative cooling chiller of the present invention;
图2为本实用新型的蒸发冷却式冷水机组第二种较优选实施例的结构示意图;Fig. 2 is the structural representation of the second preferred embodiment of the evaporative cooling chiller of the present invention;
图3为本实用新型的蒸发冷却式冷水机组第三种较优选实施例的结构示意图;Fig. 3 is the structure diagram of the third more preferred embodiment of the evaporative cooling chiller of the present invention;
图4为本实用新型的蒸发冷却式冷水机组第四种较优选实施例的结构示意图;Fig. 4 is the structure diagram of the fourth more preferred embodiment of the evaporative cooling chiller of the present utility model;
图5为本实用新型的蒸发冷却式冷水机组第五种较优选实施例的结构示意图;Fig. 5 is a structural schematic diagram of a fifth preferred embodiment of the evaporative cooling chiller of the present invention;
图6为本实用新型的蒸发式冷却装置第一种较优选结构的示意图;Fig. 6 is a schematic diagram of the first preferred structure of the evaporative cooling device of the present invention;
图7为本实用新型的蒸发式冷却装置第二种较优选结构的示意图;Fig. 7 is the schematic diagram of the second preferred structure of the evaporative cooling device of the present invention;
图8为本实用新型的蒸发式冷却装置第三种较优选结构的示意图;Fig. 8 is the schematic diagram of the third preferred structure of the evaporative cooling device of the present invention;
图9为本实用新型的蒸发式冷却装置第四种较优选结构的示意图;Fig. 9 is a schematic diagram of the fourth preferred structure of the evaporative cooling device of the present invention;
图10为本实用新型的蒸发式冷却装置第五种较优选结构的示意图;Fig. 10 is a schematic diagram of the fifth preferred structure of the evaporative cooling device of the present invention;
图11为本实用新型的蒸发式冷却装置第六种较优选结构的示意图。Fig. 11 is a schematic diagram of the sixth preferred structure of the evaporative cooling device of the present invention.
其中,图1至图11的附图标记如下:Wherein, the reference signs of Fig. 1 to Fig. 11 are as follows:
101、压缩机;102、冷凝器;1021、冷凝器的进风口;103、节流装置;104、蒸发器;1041、冷冻液进口端;1042、冷冻液出口端;105、蒸发式冷却装置;1051、冷冻液进口;1052、冷冻液出口;1053、蒸发式冷却单元;1、第一换热器;11、第一换热器的进液端;12、第一换热器的出液端;2、第二换热器;21、冷冻液管道入口;22、冷冻液管道出口;3、壳体;31、进风口;32、出风口;4、抽风机;5、冷却液喷淋器;6、冷却液循环泵;61、冷却液循环泵入口;62、冷却液循环泵出口;7、冷却液集液盘;8、冷冻液循环泵;81、冷冻液循环泵的入口;82、冷冻液循环泵的出口;9、冷冻液流量调节阀;91、冷冻液流量调节阀的入口;92、冷冻液流量调节阀的出口;A、进液口;B、出液口。101. Compressor; 102. Condenser; 1021. Air inlet of condenser; 103. Throttling device; 104. Evaporator; 1041. Refrigerant inlet; 1042. Refrigerant outlet; 105. Evaporative cooling device; 1051. Refrigerant inlet; 1052. Refrigerant outlet; 1053. Evaporative cooling unit; 1. The first heat exchanger; 11. The liquid inlet of the first heat exchanger; 12. The liquid outlet of the first heat exchanger 2, the second heat exchanger; 21, the inlet of the refrigerant pipe; 22, the outlet of the refrigerant pipe; 3, the shell; 31, the air inlet; 32, the air outlet; 4, the exhaust fan; 5, the coolant sprayer ;6. Coolant circulation pump; 61. Coolant circulation pump inlet; 62. Coolant circulation pump outlet; 7. Coolant collecting tray; 8. Refrigeration circulation pump; 81. Refrigeration circulation pump inlet; 9. The refrigerant flow regulating valve; 91. The inlet of the refrigerant flow regulating valve; 92. The outlet of the refrigerant flow regulating valve; A. Liquid inlet; B. Liquid outlet.
并且,图1至11中虚线箭头的方向为空气的流动方向。Moreover, the direction of the dotted arrows in FIGS. 1 to 11 is the flow direction of the air.
具体实施方式Detailed ways
为更进一步阐述本实用新型为达成预定实用新型目的所采取的技术手段及功效,以下结合附图及较佳实施例,对依据本实用新型的具体实施方式、结构、特征及其功效,详细说明如下:In order to further explain the technical means and effects of the utility model to achieve the intended purpose of the utility model, the specific implementation, structure, features and effects of the utility model will be described in detail below in conjunction with the accompanying drawings and preferred embodiments. as follows:
实施例1Example 1
图1所示的是本实用新型蒸发冷却式冷水机组的第一种实施方式,其包括压缩机101、冷凝器102、节流装置103、蒸发器104,所述蒸发器104设有冷冻液进口端1041和冷冻液出口端1042;所述压缩机101的排气口管道连接冷凝器102的气体管,所述冷凝器102的液体管通过所述节流装置103连接所述蒸发器104的液体管;所述蒸发器104的气体管管道连接所述压缩机101的吸气口;为了节省处理高温回水时的能耗,提高整机能效比,该蒸发冷却式冷水机组还包括蒸发式冷却装置105;所述蒸发式冷却装置设有冷冻液进口1051和冷冻液出口1052,所述冷冻液出口1052与所述冷冻液进口端1041管道相通。What Fig. 1 shows is the first embodiment of the evaporative cooling chiller of the present invention, which includes a compressor 101, a condenser 102, a throttling device 103, and an evaporator 104, and the evaporator 104 is provided with a refrigerant inlet port 1041 and refrigerant outlet port 1042; the exhaust pipe of the compressor 101 is connected to the gas pipe of the condenser 102, and the liquid pipe of the condenser 102 is connected to the liquid of the evaporator 104 through the throttling device 103 tube; the gas pipe of the evaporator 104 is connected to the suction port of the compressor 101; in order to save energy consumption when processing high-temperature return water and improve the energy efficiency ratio of the whole machine, the evaporative cooling chiller also includes evaporative cooling Device 105; the evaporative cooling device is provided with a cooling liquid inlet 1051 and a cooling liquid outlet 1052, and the cooling liquid outlet 1052 communicates with the cooling liquid inlet port 1041 through pipes.
本实用新型的蒸发冷却式冷水机组工作原理如下:The working principle of the evaporative cooling chiller of the present invention is as follows:
待降温冷冻液先从冷冻液进口1051进入到蒸发式冷却装置105内部作前置降温形成低温冷冻液后依次经过所述冷冻液出口1052、冷冻液进口端1041进入到蒸发器104中,从而为与流经蒸发器104的制冷剂换热作好准备。The refrigerated liquid to be cooled first enters the inside of the evaporative cooling device 105 from the refrigerated liquid inlet 1051 for pre-cooling to form a low-temperature refrigerated liquid, and then enters the evaporator 104 through the refrigerated liquid outlet 1052 and the refrigerated liquid inlet port 1041, thereby providing Ready to exchange heat with the refrigerant flowing through the evaporator 104 .
制冷剂经压缩机101压缩后成高温高压状态的气体时由制冷系统管道进入冷凝器102,被冷凝器102中的冷却水吸收热量后,高温高压状态的气体被冷却成低温高压液体,经节流装置103形成低温低压液体并进入蒸发器104中与冷冻液进行热交换,制取低温冷冻液,此时,在蒸发器104中的低温低压液体从输入到蒸发器内的低温冷冻液吸收热量而蒸发汽化并被压缩机101吸走,完成制冷循环模式,而低温冷冻液由于在制冷剂汽化过程中进一步失去热量而使其温度进一步降低,最后再经所述蒸发器的冷冻液出口端1042输出到用户侧,从而为用户提供更低温度的冷冻液。When the refrigerant is compressed by the compressor 101 and becomes a high-temperature and high-pressure gas, it enters the condenser 102 through the refrigeration system pipe, and after being absorbed by the cooling water in the condenser 102, the high-temperature and high-pressure gas is cooled into a low-temperature and high-pressure liquid. The flow device 103 forms a low-temperature and low-pressure liquid and enters the evaporator 104 for heat exchange with the refrigerated liquid to produce a low-temperature refrigerated liquid. At this time, the low-temperature and low-pressure liquid in the evaporator 104 absorbs heat from the low-temperature refrigerated liquid input into the evaporator The evaporation is vaporized and absorbed by the compressor 101 to complete the refrigeration cycle mode, and the temperature of the low-temperature refrigerant is further reduced due to further loss of heat during the refrigerant vaporization process, and finally passes through the refrigerant outlet port 1042 of the evaporator Output to the user side, thus providing users with lower temperature refrigerant.
由于本实用新型的蒸发冷却式冷水机组在传统的冷水机组上增设蒸发式冷却装置105,使待降温冷冻液先经过蒸发式冷却装置105作前置降温后再进入到蒸发器104中作二次降温,相对于不设有蒸发式冷却装置105只能利用蒸发器104作一次降温的传统冷水机组,能够有助于节省处理高温回水时的能耗,大大地提高了整机的能效比。Since the evaporative cooling chiller of the present utility model adds an evaporative cooling device 105 to the traditional chiller, the frozen liquid to be cooled first passes through the evaporative cooling device 105 for pre-cooling and then enters the evaporator 104 for secondary cooling. Cooling, compared to the traditional chiller that does not have the evaporative cooling device 105 and can only use the evaporator 104 for one-time cooling, can help save energy consumption when processing high-temperature return water, and greatly improve the energy efficiency ratio of the whole machine.
作为本实用新型蒸发式冷却装置105的改进方案,所述蒸发式冷却装置105包括N个蒸发式冷却单元1053,每个所述蒸发式冷却单元1053均设有进液口和出液口;所述N个蒸发式冷却单元1053的进、出液口通过管道依次串连,并且所述冷冻液进口1051为第一个蒸发式冷却单元1053的进液口,所述冷冻液出口1052为第N个蒸发式冷却单元1053的出液口;所述N为正整数。As an improved solution of the evaporative cooling device 105 of the present invention, the evaporative cooling device 105 includes N evaporative cooling units 1053, and each of the evaporative cooling units 1053 is provided with a liquid inlet and a liquid outlet; The liquid inlets and outlets of the N evaporative cooling units 1053 are sequentially connected in series through pipelines, and the refrigerant inlet 1051 is the liquid inlet of the first evaporative cooling unit 1053, and the refrigerant outlet 1052 is the Nth liquid outlets of evaporative cooling units 1053; said N is a positive integer.
采用蒸发式冷却装置改进方案后,冷冻液的降温过程是:待降温冷冻液经第一级蒸发式冷却单元1053的进液口进入第一级蒸发式冷却单元1053内冷却降温,再经第一级蒸发式冷却单元1053的出液口进入第二、三……级蒸发式冷却单元至第N级蒸发式冷却单元1053降温后到达蒸发器的冷冻液进口端1041,经该蒸发器冷却至目标温度后再经蒸发器的冷冻液出口端1042为用户提供低温冷冻液。需要说明的是,当所述N的取值越大时,所述蒸发式冷却装置105的换热效率就越高,从而使本实用新型的蒸发冷却式冷水机组的换热效率就越高。After adopting the improvement plan of the evaporative cooling device, the cooling process of the refrigerated liquid is: the refrigerated liquid to be cooled enters the liquid inlet of the first-stage evaporative cooling unit 1053 to cool down in the first-stage evaporative cooling unit 1053, and then passes through the first-stage evaporative cooling unit 1053 to cool down. The liquid outlet of the first-stage evaporative cooling unit 1053 enters the second, third, ... stage evaporative cooling units until the Nth-stage evaporative cooling unit 1053 cools down and reaches the refrigerant inlet port 1041 of the evaporator, and is cooled to the target by the evaporator. After the temperature is reached, the cryogenic liquid is provided to the user through the refrigerant liquid outlet port 1042 of the evaporator. It should be noted that when the value of N is larger, the heat exchange efficiency of the evaporative cooling device 105 is higher, so that the heat exchange efficiency of the evaporative cooling water chiller of the present utility model is higher.
作为本实用新型蒸发式冷却装置的进一步改进,如图6所示,所述蒸发式冷却单元1053的第一种优选结构为:所述蒸发式冷却单元1053还包括壳体3,设于壳体3顶部出风口32上的抽风机4,设于壳体3侧面进风口31中的第一换热器1,设于壳体3内的冷却液集液盘7和冷却液循环泵6,以及设于壳体3内且位于连通所述进风口31与抽风机4的风道之中的冷却液喷淋器5和第二换热器2;所述冷却液喷淋器5和冷却液集液盘7分别位于第二换热器2上方和下方;所述第一换热器1为气-液换热器;所述第二换热器2至少设有冷冻液管道;进液口A、第一换热器进液端11、第一换热器出液端12、冷冻液管道入口21、冷冻液管道出口22、出液口B依次管道相通;所述冷却液循环泵入口61管道连通所述冷却液集液盘7,冷却液循环泵出口62管道连通所述冷却液喷淋器5。As a further improvement of the evaporative cooling device of the present invention, as shown in FIG. 6, the first preferred structure of the evaporative cooling unit 1053 is: the evaporative cooling unit 1053 also includes a housing 3, which is located in the housing 3 The exhaust fan 4 on the top air outlet 32, the first heat exchanger 1 arranged in the side air inlet 31 of the casing 3, the cooling liquid collecting pan 7 and the cooling liquid circulation pump 6 arranged in the casing 3, and The cooling liquid sprayer 5 and the second heat exchanger 2 which are arranged in the housing 3 and are located in the air duct connecting the air inlet 31 and the exhaust fan 4; the cooling liquid sprayer 5 and the cooling liquid collection The liquid pan 7 is respectively located above and below the second heat exchanger 2; the first heat exchanger 1 is a gas-liquid heat exchanger; the second heat exchanger 2 is at least provided with a cooling liquid pipeline; the liquid inlet A , the liquid inlet end 11 of the first heat exchanger, the liquid outlet end 12 of the first heat exchanger, the inlet 21 of the refrigerant pipe, the outlet 22 of the refrigerant pipe, and the outlet B are connected in sequence; the inlet 61 of the cooling liquid circulation pump is piped The cooling liquid collecting pan 7 is connected, and the cooling liquid circulation pump outlet 62 is connected to the cooling liquid sprayer 5 through pipelines.
需要说明的是,所述第一换热器1的数量为一个或多个,所述进风口31与所述第一换热器1一一对应,对应的第一换热器1设置在对应进风口31之中;所述第二换热器2的数量为一个或多个。而为了简化结构,本实施例中所述第一换热器1和第二换热器2的数量分别为一。同时,为了节约生产成本,提高生产效益,所述第一换热器1为翅片式换热器或微通道式换热器中的任何一种;所述第二换热器2为微通道式换热器或蛇形管式换热器或板片式换热器或板管式换热器中的任何一种。It should be noted that the number of the first heat exchangers 1 is one or more, the air inlets 31 correspond to the first heat exchangers 1 one by one, and the corresponding first heat exchangers 1 are arranged at the corresponding Among the air inlets 31; the number of the second heat exchanger 2 is one or more. In order to simplify the structure, the number of the first heat exchanger 1 and the number of the second heat exchanger 2 in this embodiment is one respectively. At the same time, in order to save production costs and improve production efficiency, the first heat exchanger 1 is any one of a finned heat exchanger or a microchannel heat exchanger; the second heat exchanger 2 is a microchannel Any one of type heat exchanger or serpentine tube heat exchanger or plate-fin heat exchanger or plate-tube heat exchanger.
上述蒸发式冷却单元的工作原理如下:The evaporative cooling unit described above works as follows:
待降温的冷冻液依次经第一级蒸发式冷却单元1053的进液口A、第一换热器的进液端11进入到第一换热器1内,并在抽风机4作用下与第一换热器1周围的常温空气进行热交换,该待降温的冷冻液吸收了常温空气的热量后被加热成高温冷冻液后进入第二换热器2的冷冻液管道内,而该常温空气因失去热量而被冷却成低温空气并向第二换热器2的方向流动从而为与冷却液喷淋器5所喷出的冷却液进行逆程质传递换热作准备;The refrigerant to be cooled enters the first heat exchanger 1 through the liquid inlet A of the first-stage evaporative cooling unit 1053 and the liquid inlet 11 of the first heat exchanger in sequence, and is combined with the first heat exchanger 1 under the action of the exhaust fan 4 The normal-temperature air around the heat exchanger 1 performs heat exchange. After absorbing the heat of the normal-temperature air, the refrigerant to be cooled is heated into a high-temperature refrigerant and then enters the refrigerant pipeline of the second heat exchanger 2. The normal-temperature air Due to the loss of heat, it is cooled into low-temperature air and flows in the direction of the second heat exchanger 2 so as to prepare for reverse mass transfer and heat exchange with the coolant sprayed from the coolant sprayer 5;
冷却液喷淋器5中的冷却液喷淋到第二换热器2的表面上,部分冷却液被蒸发并与该低温空气接触后即被冷却,冷却后的被蒸发冷却液的理论极限温度是空气的露点温度,冷却后的被蒸发冷却液再与未被蒸发的冷却液发生热交换使该未被蒸发的冷却液降温,降温后的未被蒸发的冷却液的理论极限温度也是空气的露点温度;在第二换热器2表面上的未被蒸发的冷却液在被蒸发冷却液降温的同时也和第二换热器2的冷冻液管道内部流动的高温冷冻液进行热交换,使得第二换热器2内的高温冷冻液被降温成低温冷冻液,而该低温冷冻液的理论极限温度也是空气的露点温度,最后该低温冷冻液后经出液口输出到蒸发器的冷冻液进口端(即当N的取值为1时)或者进入下一级的蒸发式冷却单元1053的进液口(即当N的取值为2以上时);The coolant in the coolant sprayer 5 is sprayed onto the surface of the second heat exchanger 2, part of the coolant is evaporated and cooled after contacting the low-temperature air, and the theoretical limit temperature of the evaporated coolant after cooling is It is the dew point temperature of the air. After cooling, the evaporating cooling liquid exchanges heat with the non-evaporating cooling liquid to lower the temperature of the non-evaporating cooling liquid. The theoretical limit temperature of the non-evaporating cooling liquid after cooling is also that of air. Dew point temperature; the non-evaporated cooling liquid on the surface of the second heat exchanger 2 is cooled by the evaporative cooling liquid while also exchanging heat with the high-temperature refrigerating liquid flowing inside the refrigerating liquid pipeline of the second heat exchanger 2, so that The high-temperature refrigerant in the second heat exchanger 2 is cooled to a low-temperature refrigerant, and the theoretical limit temperature of the low-temperature refrigerant is also the dew point temperature of the air. Finally, the low-temperature refrigerant is output to the refrigerant of the evaporator through the liquid outlet. The inlet port (that is, when the value of N is 1) or the liquid inlet of the next-stage evaporative cooling unit 1053 (that is, when the value of N is more than 2);
最后,在第二换热器2下方的未被蒸发的冷却液继续和被蒸发的冷却液换热降温直至落回到冷却液集液盘7中,并在冷却液循环泵6的作用下重新抽送到冷却液喷淋器5中以作循环使用;Finally, the non-evaporated cooling liquid below the second heat exchanger 2 continues to exchange heat with the evaporated cooling liquid until it falls back into the cooling liquid collecting pan 7, and is redistributed under the action of the cooling liquid circulation pump 6. pumped into the coolant sprayer 5 for recycling;
而抽风机4强制吸入的室外空气在经第一换热器1降温后再在装置内与自上而下喷淋的冷却液逆流接触,使得冷却液加快蒸发,利用冷却液的蒸发潜热带走第二换热器2内冷冻液的热量以及第二换热器2外部冷却液的热量,空气由于冷却液的蒸发被冷却加湿成低温高湿空气被抽风机4排放至大气中。The outdoor air that is forcibly inhaled by the exhaust fan 4 is cooled by the first heat exchanger 1 and then in countercurrent contact with the cooling liquid sprayed from top to bottom in the device, so that the cooling liquid evaporates quickly, and the latent heat of evaporation of the cooling liquid is used to take away The heat of the refrigerant liquid in the second heat exchanger 2 and the heat of the cooling liquid outside the second heat exchanger 2, the air is cooled and humidified by the evaporation of the cooling liquid to become low-temperature and high-humidity air, which is discharged into the atmosphere by the exhaust fan 4 .
本实用新型的蒸发式冷却单元的具体结构,使冷冻液在进液口A、第一换热器1、第二换热器2、出液口B之间的管道内流动,结合先采用喷淋的冷却液直接与吸入壳体3内部的被冷却空气进行换热、再由喷淋的冷却液与第二换热器2内流动的冷冻液进行换热的间接传热方式,在实现对冷冻液降温的同时还避免了冷冻液直接接触空气,防止空气中的灰尘颗粒污染所制得的低温冷冻液,从而避免出现因低温冷冻液内的灰尘颗粒造成蒸发器104或下一级蒸发式冷冻单元1053的管道堵塞现象,也避免出现所制取的低温冷冻液在返回单元内部时造成单元管道堵塞的现象,延长了本实用新型蒸发式冷却装置的使用寿命。The specific structure of the evaporative cooling unit of the utility model makes the refrigerant flow in the pipeline between the liquid inlet A, the first heat exchanger 1, the second heat exchanger 2, and the liquid outlet B, combined with the first spray The sprayed cooling liquid directly exchanges heat with the cooled air sucked into the housing 3, and then the sprayed cooling liquid exchanges heat with the cooling liquid flowing in the second heat exchanger 2. While cooling the refrigerant liquid, it also avoids direct contact of the refrigerant liquid with the air, and prevents dust particles in the air from contaminating the prepared cryogenic refrigerant, thus avoiding the occurrence of dust particles in the cryogenic refrigerant causing the evaporator 104 or the next-stage evaporative The pipe blockage of the freezing unit 1053 also avoids the blockage of the unit pipes caused by the produced low-temperature refrigerated liquid returning to the inside of the unit, prolonging the service life of the evaporative cooling device of the present invention.
并且,为了满足用户对空调水的制冷需求,作为本实施例的进一步改进,进入所述进液口A的冷冻液为空调系统的回水、空调系统的供水、以及回水经过冷却后中间过程的空调水三者中的一种或两种以上。而且,需要说明的是,所述冷却液可以为水或者除水以外能够用于对物体降温的任何液体。Moreover, in order to meet the user's cooling demand for air-conditioning water, as a further improvement of this embodiment, the refrigerant entering the liquid inlet A is the return water of the air-conditioning system, the water supply of the air-conditioning system, and the intermediate process after the return water is cooled. One or more of the three types of air-conditioning water. Moreover, it should be noted that the cooling liquid may be water or any liquid other than water that can be used to cool down objects.
而作为本实施例更进一步改进,所述冷凝器102为蒸发式冷凝器,由于蒸发式冷却器散热性能优越,系统制冷系数大,并且无需冷却水塔,所以不但节约了安装空间,而且还可降低冷水机组的制冷剂循环量,使本实用新型的蒸发冷却式冷水机组能起到了节能的优越效果,满足了消费者对产品节能环保的使用需求。As a further improvement of this embodiment, the condenser 102 is an evaporative condenser. Since the evaporative cooler has superior heat dissipation performance, the system has a large refrigeration coefficient, and does not require a cooling tower, it not only saves installation space, but also reduces The refrigerant circulation volume of the chiller enables the evaporative cooling chiller of the utility model to achieve the superior effect of energy saving, and meets the consumer's demand for energy-saving and environment-friendly products.
实施例2Example 2
图2所示的是本实用新型蒸发冷却式冷水机组的第二种实施方式,其与图1所示的第一种实施方式的不同点在于:所述N为2以上的正整数,所述蒸发式冷却单元1053的出风口32部分或全部连通所述蒸发式冷凝器的进风口1021。由蒸发式冷却单元1053排出的经冷却的空气,能使蒸发式冷凝器的进风温度比一般的环境温度要低,使蒸发式冷凝器的换热性能更优,从而使本实用新型的蒸发冷却式冷水机组整体起到了节能的优越效果。What Fig. 2 shows is the second embodiment of the evaporative cooling water chiller of the utility model, which differs from the first embodiment shown in Fig. 1 in that: said N is a positive integer greater than 2, said Part or all of the air outlet 32 of the evaporative cooling unit 1053 communicates with the air inlet 1021 of the evaporative condenser. The cooled air discharged from the evaporative cooling unit 1053 can make the air inlet temperature of the evaporative condenser lower than the general ambient temperature, so that the heat transfer performance of the evaporative condenser is better, so that the evaporation of the utility model The cooling chiller has a superior effect of energy saving as a whole.
实施例3Example 3
图3所示的本实用新型蒸发冷却式冷水机组的第三种实施方式,其与图1所示的第一种实施方式的不同点在于:所述冷凝器102为风冷式冷凝器。由于风冷式冷凝器的运行维护最简单,设备投资少,适合应用在水资源缺乏的地区,对于机组需要年运行时间长的地区,其经济效益更明显,从而使本实用新型的蒸发冷却式冷水机组整体起到了节能的优越效果。The third embodiment of the evaporative cooling water chiller of the present invention shown in FIG. 3 differs from the first embodiment shown in FIG. 1 in that the condenser 102 is an air-cooled condenser. Since the operation and maintenance of the air-cooled condenser is the simplest and the equipment investment is small, it is suitable for use in areas where water resources are scarce. For areas where the unit needs to run for a long time, its economic benefits are more obvious, so that the evaporative cooling of the utility model The chiller has a superior effect of energy saving as a whole.
实施例4Example 4
图4所示的是本实用新型蒸发冷却式冷水机组的第四种实施方式,其与图3所示的第三种实施方式的不同点在于:所述N为2以上的正整数,所述蒸发式冷却单元1053的出风口32部分或全部连通所述风冷式冷凝器的进风口1021。由蒸发式冷却单元1053排出的经冷却的空气,能使风冷式冷凝器的进风温度比一般的环境温度要低,使风冷式冷凝器的换热性能更优,从而使本实用新型的蒸发冷却式冷水机组整体起到了节能的优越效果。What Fig. 4 shows is the fourth embodiment of the evaporative cooling water chiller of the present utility model, which is different from the third embodiment shown in Fig. 3 in that: said N is a positive integer greater than 2, said Part or all of the air outlet 32 of the evaporative cooling unit 1053 communicates with the air inlet 1021 of the air-cooled condenser. The cooled air discharged from the evaporative cooling unit 1053 can make the inlet air temperature of the air-cooled condenser lower than the general ambient temperature, so that the heat exchange performance of the air-cooled condenser is better, so that the utility model The evaporative cooling chiller has a superior effect of energy saving as a whole.
实施例5Example 5
图5所示的是本实用新型蒸发冷却式冷水机组的第五种实施方式,其与图1所示的第一种实施方式的不同点在于:所述冷凝器102为水冷式冷凝器。由于水冷式冷凝器具备成熟的冷凝技术,所以能使本实用新型的蒸发冷却式冷水机组能更加稳定地运作。Fig. 5 shows the fifth embodiment of the evaporative cooling water chiller of the present invention, which differs from the first embodiment shown in Fig. 1 in that the condenser 102 is a water-cooled condenser. Since the water-cooled condenser has mature condensation technology, the evaporative cooling chiller of the utility model can operate more stably.
上述实施例1至实施例5所述的蒸发冷却式冷水机组的蒸发式冷却单元1053的结构可以采用如下5种优选结构作为替换:The structure of the evaporative cooling unit 1053 of the evaporative cooling chiller described in the above embodiments 1 to 5 can be replaced by the following five preferred structures:
优选结构2Preferred structure 2
图7所示的是本实用新型蒸发式冷却单元1053的第二种优选结构,其与图6所示的第一种优选结构的区别点在于:该蒸发式冷却单元1053还包括冷冻液循环泵8,该冷冻液循环泵的入口81管道连通所述出液口B,该冷冻液循环泵的出口82管道连通所述进液口A,从而使所制得的低温冷冻液分成两路,一路流向出液口B输出到蒸发器的冷冻液进口端(即当N的取值为1时)或者进入下一级蒸发式冷却单元的进液口(即当N的取值为2以上时),另一路则能够重新注入到蒸发式冷却单元内,进一步降低冷冻液进口A处的冷冻液温度,使第一换热器1内的冷冻液需要向第一换热器1周围的空气吸收更多的热量才能升高温度,以达到进一步降低第一换热器1周围空气温度的目的,而当这部分空气被抽风机4抽入到壳体3内部时,则可加快其对喷淋出来的冷却液的冷却作用,最终加快第二换热器2内的冷冻液的冷却速度,大大地提高了蒸发式冷却单元的换热效率,最终达到提高本实用新型蒸发冷却式冷水机组整体换热效率的目的。What Fig. 7 shows is the second preferred structure of the evaporative cooling unit 1053 of the present utility model, which differs from the first preferred structure shown in Fig. 6 in that: the evaporative cooling unit 1053 also includes a refrigerant circulation pump 8. The inlet 81 of the cooling liquid circulating pump is connected to the liquid outlet B, and the outlet 82 of the cooling liquid circulating pump is connected to the liquid inlet A, so that the prepared low-temperature cooling liquid is divided into two paths, one path Flow to the liquid outlet B and output to the refrigerant inlet port of the evaporator (that is, when the value of N is 1) or enter the liquid inlet of the next-stage evaporative cooling unit (that is, when the value of N is more than 2) , the other way can be re-injected into the evaporative cooling unit to further reduce the temperature of the refrigerant at the inlet A of the refrigerant, so that the refrigerant in the first heat exchanger 1 needs to absorb more into the air around the first heat exchanger 1 More heat can increase the temperature, so as to further reduce the temperature of the air around the first heat exchanger 1, and when this part of air is sucked into the shell 3 by the exhaust fan 4, it can be sprayed out quickly. The cooling effect of the cooling liquid finally accelerates the cooling speed of the freezing liquid in the second heat exchanger 2, greatly improves the heat exchange efficiency of the evaporative cooling unit, and finally achieves the improvement of the overall heat exchange of the evaporative cooling water chiller of the utility model purpose of efficiency.
优选结构3Preferred structure 3
图8所示的是本实用新型蒸发式冷却单元1053的第三种优选结构,其与图6所示的第一种优选结构的区别点在于:本优选结构增设多了一个第一换热器1,具体是:所述第一换热器1数量为二,所述壳体3侧面的进风口31数量为二;所述两个第一换热器1分别对应安装在所述两个进风口31中;所述两个第一换热器的进液端11连通进液口A,所述两个第一换热器的出液端12连通所述第二换热器2的冷冻液管道入口21。What Fig. 8 shows is the third preferred structure of the evaporative cooling unit 1053 of the present invention, and the difference between it and the first preferred structure shown in Fig. 6 is that this preferred structure adds a first heat exchanger 1. Specifically: the number of the first heat exchangers 1 is two, and the number of air inlets 31 on the side of the housing 3 is two; the two first heat exchangers 1 are respectively installed in the two inlets. In the tuyere 31; the liquid inlet ports 11 of the two first heat exchangers are connected to the liquid inlet A, and the liquid outlet ports 12 of the two first heat exchangers are connected to the refrigerant of the second heat exchanger 2 Pipe inlet 21.
冷冻液在蒸发式冷却单元1053内的具体流向是:待降温的冷冻液经进液口A进入本实用新型蒸发式冷却单元后分为两路分别流到所述两个第一换热器1中与被抽风机4强制吸入的室外空气换热,冷冻液升温,再送入冷却液喷淋器5下部的第二换热器2的冷冻液管道内被冷却,被冷却后的冷冻液经本实用新型的蒸发式冷却单元的出液口B输出到蒸发器的冷冻液进口端(即当N的取值为1时)或者进入下一级蒸发式冷却单元的进液口(即当N的取值为2以上时)。The specific flow direction of the refrigerated liquid in the evaporative cooling unit 1053 is: the refrigerated liquid to be cooled enters the evaporative cooling unit of the utility model through the liquid inlet A and is divided into two paths and flows to the two first heat exchangers 1 respectively. Exchange heat with the outdoor air that is forcibly inhaled by the exhaust fan 4, the refrigerant heats up, and then is sent to the refrigerant pipe of the second heat exchanger 2 at the lower part of the coolant sprayer 5 to be cooled, and the cooled refrigerant passes through this The liquid outlet B of the evaporative cooling unit of the utility model is output to the refrigerant inlet port of the evaporator (that is, when the value of N is 1) or enters the liquid inlet of the next-stage evaporative cooling unit (that is, when the value of N is 1) when the value is greater than 2).
本优选结构与只采用一个第一换热器1的第一种优选结构相比,使壳体3内有多一倍的冷低温空气流向第二换热器2,从而使第二换热器2内的冷冻液可以更快地被降温到目标温度上,大大地提高了第二换热器2的换热效率,从而提高了蒸发式冷却单元的换热效率,最终达到提高本实用新型蒸发冷却式冷水机组整体换热效率的目的。Compared with the first preferred structure using only one first heat exchanger 1, this preferred structure makes twice as much cold and low-temperature air in the housing 3 flow to the second heat exchanger 2, so that the second heat exchanger The refrigerated liquid in 2 can be cooled to the target temperature faster, which greatly improves the heat exchange efficiency of the second heat exchanger 2, thereby improving the heat exchange efficiency of the evaporative cooling unit, and finally achieving the improvement of the evaporation rate of the utility model. The purpose of the overall heat transfer efficiency of the cooled chiller.
优选结构4Preferred structure 4
图9所示的是本实用新型蒸发式冷却单元1053的第四种优选结构,其与图6所示的第一种优选结构的区别点有两个。Figure 9 shows the fourth preferred structure of the evaporative cooling unit 1053 of the present invention, which differs from the first preferred structure shown in Figure 6 in two points.
第一个区别点是:本优选结构的第二换热器2数量为二;其中,第一个第二换热器2的冷冻液管道入口21与出口22分别对应连通第一换热器的出液端12与第二个第二换热器的冷冻液管道入口21,所述第二个第二换热器2的冷冻液管道出口22连通所述出液口B。为了使结构更加紧凑,所述两个第二换热器2沿上下方向排列,并且所述第一个第二换热器2位于冷却液喷淋器5的下方,所述第二个第二换热器2位于所述第一个第二换热器2的下方。The first point of difference is: the number of second heat exchangers 2 in this preferred structure is two; wherein, the refrigerant liquid pipeline inlet 21 and outlet 22 of the first second heat exchanger 2 are respectively connected to the first heat exchanger. The liquid outlet 12 communicates with the liquid outlet B with the refrigerant liquid pipe inlet 21 of the second second heat exchanger, and the refrigerant liquid pipe outlet 22 of the second second heat exchanger 2 . In order to make the structure more compact, the two second heat exchangers 2 are arranged up and down, and the first second heat exchanger 2 is located below the coolant sprayer 5, and the second second heat exchanger 2 The heat exchanger 2 is located below the first and second heat exchangers 2 .
冷冻液在蒸发式冷却单元1053内的具体流向是:待降温的冷冻液经进液口A进入本实用新型蒸发式冷却单元1053后流到所述第一换热器1中与被抽风机4强制吸入的室外空气换热,冷冻液升温,再送入冷却液喷淋器5下部的所述第一个第二换热器2的冷冻液管道内被冷却,被冷却后的冷冻液再送入所述第二个第二换热器2的冷冻液管道内进行二次冷却,最后再经本实用新型的蒸发式冷却单元的出液口B输出到蒸发器的冷冻液进口端(即当N的取值为1时)或者进入下一级蒸发式冷却单元的进液口(即当N的取值为2以上时)。The specific flow direction of the refrigerated liquid in the evaporative cooling unit 1053 is: the refrigerated liquid to be cooled enters the evaporative cooling unit 1053 of the utility model through the liquid inlet A, and then flows into the first heat exchanger 1 and is connected with the exhaust fan 4. The forced inhaled outdoor air is heat-exchanged, and the refrigerant heats up, and then sent into the refrigerant pipeline of the first and second heat exchangers 2 at the bottom of the coolant sprayer 5 to be cooled, and the cooled refrigerant is then sent to the Secondary cooling is carried out in the freezing liquid pipeline of the second second heat exchanger 2, and finally output to the freezing liquid inlet port of the evaporator through the liquid outlet B of the evaporative cooling unit of the present utility model (that is, when N when the value is 1) or into the liquid inlet of the next-stage evaporative cooling unit (that is, when the value of N is more than 2).
相对于只采用一个第二换热器2的第一种优选结构,本实施例使用了两个第二换热器2,使第一换热器出液端12输出的冷冻液进行二次冷却,从而使冷冻液更快地被降温到目标温度上,大大地提高了本实用新型蒸发式冷却单元的换热效率,最终达到提高本实用新型蒸发冷却式冷水机组整体换热效率的目的。Compared with the first preferred structure using only one second heat exchanger 2, this embodiment uses two second heat exchangers 2, so that the refrigerant output from the liquid outlet 12 of the first heat exchanger is subjected to secondary cooling , so that the refrigerant is cooled to the target temperature faster, greatly improving the heat exchange efficiency of the evaporative cooling unit of the utility model, and finally achieving the purpose of improving the overall heat exchange efficiency of the evaporative cooling chiller of the utility model.
第二个区别点是:本优选结构还包括冷冻液循环泵8,冷冻液循环泵的入口81管道连通所述第一个第二换热器2的冷冻液管道出口22,冷冻液循环泵的出口82管道连通所述进液口A,从而使第一个第二换热器2所制得的低温冷冻液分成两路,一路流向第二个第二换热器2以作二次冷却,另一路则能够重新注入到蒸发式冷却单元内,进一步降低进液口A处的冷冻液温度,使第一换热器1内的冷冻液需要向第一换热器1周围的空气吸收更多的热量才能升高温度,以达到进一步降低第一换热器1周围空气温度的目的,而当这部分空气被抽风机4抽入到壳体3内部时,则可加快其对喷淋出来的冷却液的冷却作用,最终进一步加快第二换热器2内的冷冻液的冷却速度,提高了蒸发式冷却单元的换热效率,最终达到更进一步提高本实用新型蒸发冷却式冷水机组整体换热效率的目的。The second point of difference is: this preferred structure also includes a cooling liquid circulation pump 8, the inlet 81 of the cooling liquid circulation pump is connected to the cooling liquid pipeline outlet 22 of the first second heat exchanger 2, and the cooling liquid circulation pump The outlet 82 pipe is connected to the liquid inlet A, so that the low-temperature refrigerant produced by the first second heat exchanger 2 is divided into two paths, and one path flows to the second second heat exchanger 2 for secondary cooling. The other way can be re-injected into the evaporative cooling unit to further reduce the temperature of the refrigerant at the liquid inlet A, so that the refrigerant in the first heat exchanger 1 needs to absorb more into the air around the first heat exchanger 1 Only by using the heat can the temperature be raised to achieve the purpose of further reducing the temperature of the air around the first heat exchanger 1, and when this part of the air is sucked into the shell 3 by the exhaust fan 4, it can speed up its spraying process. The cooling effect of the cooling liquid further accelerates the cooling speed of the freezing liquid in the second heat exchanger 2, improves the heat exchange efficiency of the evaporative cooling unit, and finally achieves a further improvement in the overall heat exchange of the evaporative cooling water chiller of the utility model. purpose of efficiency.
优选结构5Preferred structure 5
图10所示的是本实用新型蒸发式冷却单元1053的第五种优选结构,其与图8所示的第三种优化结构的区别点有两个。FIG. 10 shows the fifth preferred structure of the evaporative cooling unit 1053 of the present invention, which differs from the third optimized structure shown in FIG. 8 in two points.
第一个区别点是:所述进液口A管道连通所述第一换热器的出液端12,以将进液口A处的冷冻液直接引导到第一换热器的出液端12处,从而降低流入第二换热器2的冷冻液管道内冷冻液的温度,提高了第二换热器2的换热效率,提高了蒸发式冷却单元1053的换热效率,从而实现提高本实用新型蒸发冷却式冷水机组整体换热效率的目的。The first difference is: the liquid inlet A pipe is connected to the liquid outlet 12 of the first heat exchanger, so as to guide the refrigerant at the liquid inlet A directly to the liquid outlet of the first heat exchanger 12, thereby reducing the temperature of the refrigerant in the refrigerant pipe flowing into the second heat exchanger 2, improving the heat exchange efficiency of the second heat exchanger 2, and improving the heat exchange efficiency of the evaporative cooling unit 1053, thereby achieving an improvement The purpose of the overall heat exchange efficiency of the evaporative cooling water chiller of the utility model.
进一步地,本优选结构还包括冷冻液流量调节阀9,所述进液口A管道连通所述冷冻液流量调节阀的入口91,所述冷冻液流量调节阀的出口92管道连通所述第一换热器的出液端12,通过设置所述冷冻液流量调节阀9,从而可以控制直接引导到第一换热器出液端12的进液口处的冷冻液的流量大小,从而实现调节第二换热器2换热效率的功能,满足使用者对蒸发式冷却单元功能多样化的使用需求。Further, this preferred structure also includes a refrigerant flow regulating valve 9, the liquid inlet A pipe is connected to the inlet 91 of the refrigerant flow regulating valve, and the outlet 92 of the refrigerant flow regulating valve is piped to the first The liquid outlet 12 of the heat exchanger, by setting the refrigerant flow regulating valve 9, can control the flow rate of the refrigerant directly directed to the liquid inlet of the first heat exchanger outlet 12, thereby realizing regulation The function of the heat exchange efficiency of the second heat exchanger 2 satisfies the user's demand for diversified functions of the evaporative cooling unit.
第二个区别点是:本优选结构还包括冷冻液循环泵8,该冷冻液循环泵的入口81管道连通所述出液口B,该冷冻液循环泵的出口82管道连通所述进液口A,从而使所制得的低温冷冻液分成两路,一路流向出液口B以输出到蒸发器的冷冻液进口端(即当N的取值为1时)或者进入下一级蒸发式冷却单元的进液口(即当N的取值为2以上时),另一路则能够重新注入到蒸发式冷却单元内,进一步降低进液口A处的冷冻液温度;一方面使第一换热器1内的冷冻液需要向第一换热器1周围的空气吸收更多的热量才能升高温度,以达到进一步降低第一换热器1周围空气温度的目的,而当这部分空气被抽风机4抽入到壳体3内部时,则可加快其对喷淋出来的冷却液的冷却作用,最终加快第二换热器2内的冷冻液的冷却速度,提高了蒸发式冷却单元的换热效率;另一方面因上述第一个区别点的存在,则可进一步降低流入第二换热器2的冷冻液管道内冷冻液的温度,进一步提高第二换热器2的换热效率,因而可进一步提高蒸发式冷却单元的换热效率,从而大大地提高了本实用新型蒸发冷却式冷水机组整体换热效率。The second difference is: this preferred structure also includes a refrigerant circulation pump 8, the inlet 81 of the refrigerant circulation pump is connected to the liquid outlet B, and the outlet 82 of the refrigerant circulation pump is connected to the liquid inlet A, so that the prepared low-temperature freezing liquid is divided into two paths, one way flows to the liquid outlet B to be output to the freezing liquid inlet port of the evaporator (that is, when the value of N is 1) or enter the next stage of evaporative cooling The liquid inlet of the unit (that is, when the value of N is more than 2), the other way can be re-injected into the evaporative cooling unit to further reduce the temperature of the refrigerant at the liquid inlet A; on the one hand, the first heat exchange The refrigerant in the device 1 needs to absorb more heat from the air around the first heat exchanger 1 to increase its temperature, so as to further reduce the temperature of the air around the first heat exchanger 1, and when this part of the air is drawn When the heat exchanger 4 is drawn into the housing 3, it can speed up its cooling effect on the sprayed coolant, and finally accelerate the cooling speed of the coolant in the second heat exchanger 2, improving the exchange rate of the evaporative cooling unit. thermal efficiency; on the other hand, due to the existence of the above-mentioned first difference point, the temperature of the refrigerated liquid in the refrigerated liquid pipeline flowing into the second heat exchanger 2 can be further reduced, and the heat exchange efficiency of the second heat exchanger 2 can be further improved. Therefore, the heat exchange efficiency of the evaporative cooling unit can be further improved, thereby greatly improving the overall heat exchange efficiency of the evaporative cooling water chiller of the utility model.
优选结构6Preferred Structure 6
图11是本实用新型的蒸发式冷却单元1053的第六种优选结构,其与图6所示的第一种优选结构相比的区别点有两个。Fig. 11 is a sixth preferred structure of the evaporative cooling unit 1053 of the present invention, which differs from the first preferred structure shown in Fig. 6 in two points.
第一个区别点是:所述第一换热器1和第二换热器2的数量分别为二;所述壳体3侧面的进风口31数量为二;所述两个第一换热器1分别对应安装在所述两个进风口31中;所述两个第一换热器的进液端11连通进液口A,所述两个第一换热器的出液端12连通第一个第二换热器2的冷冻液管道入口21,所述第一个第二换热器2的冷冻液管道出口22连通第二个第二换热器2的冷冻液管道入口21,所述第二个第二换热器2的冷冻液管道出口22连通所述出液口B。为了使结构更加紧凑,所述两个第二换热器2沿上下方向排列,并且所述第一个第二换热器2位于冷却液喷淋器5的下方,所述第二个第二换热器2位于所述第一个第二换热器2的下方。The first difference is: the number of the first heat exchanger 1 and the second heat exchanger 2 are two respectively; the number of air inlets 31 on the side of the housing 3 is two; the two first heat exchangers The device 1 is respectively installed in the two air inlets 31 correspondingly; the liquid inlets 11 of the two first heat exchangers are connected to the liquid inlet A, and the liquid outlets 12 of the two first heat exchangers are connected to each other. The coolant pipeline inlet 21 of the first second heat exchanger 2, the coolant pipeline outlet 22 of the first second heat exchanger 2 communicates with the coolant pipeline inlet 21 of the second second heat exchanger 2, The cooling liquid pipeline outlet 22 of the second second heat exchanger 2 communicates with the liquid outlet B. In order to make the structure more compact, the two second heat exchangers 2 are arranged up and down, and the first second heat exchanger 2 is located below the coolant sprayer 5, and the second second heat exchanger 2 The heat exchanger 2 is located below the first and second heat exchangers 2 .
冷冻液在蒸发式冷却单元内的具体流向是:待降温的冷冻液经进液口A进入蒸发式冷却单元后分成两路流到所述两个第一换热器1中与被抽风机4强制吸入的室外空气换热,冷冻液升温,再送入冷却液喷淋器5下部的所述第一个第二换热器2的冷冻液管道内被冷却,被冷却后的冷冻液再送入所述第二个第二换热器2的冷冻液管道内进行二次冷却,最后再经蒸发式冷却单元的出液口B以输出到蒸发器的冷冻液进口端(即当N的取值为1时)或者进入下一级蒸发式冷却单元的进液口(即当N的取值为2以上时)。The specific flow direction of the refrigerated liquid in the evaporative cooling unit is: the refrigerated liquid to be cooled enters the evaporative cooling unit through the liquid inlet A and then divides into two paths to flow into the two first heat exchangers 1 and the exhaust fan 4. The forced inhaled outdoor air is heat-exchanged, and the refrigerant heats up, and then sent into the refrigerant pipeline of the first and second heat exchangers 2 at the bottom of the coolant sprayer 5 to be cooled, and the cooled refrigerant is then sent to the Secondary cooling is carried out in the refrigerant liquid pipeline of the second second heat exchanger 2, and finally through the liquid outlet B of the evaporative cooling unit to output to the refrigerant inlet port of the evaporator (that is, when the value of N is 1) or into the liquid inlet of the next-stage evaporative cooling unit (that is, when the value of N is above 2).
本优选结构与只采用一个第一换热器1和一个第二换热器2的第一种优选结构相比,一方面使用两个第一换热器1可使壳体3内有多一倍的冷低温空气流向第二换热器2,大大地提高了第二换热器2的换热效率,另一方面使用了两个第二换热器2,使两个第一换热器的出液端12输出的冷冻液进行二次冷却,从而使冷冻液更快地被降温到目标温度上,大大地提高了蒸发式冷却单元的换热效率,最终达到提高本实用新型蒸发冷却式冷水机组整体换热效率的目的。Compared with the first preferred structure using only one first heat exchanger 1 and one second heat exchanger 2, this preferred structure uses two first heat exchangers 1 on the one hand to make the shell 3 have more Double the cold and low temperature air flows to the second heat exchanger 2, which greatly improves the heat exchange efficiency of the second heat exchanger 2. On the other hand, two second heat exchangers 2 are used to make the two first heat exchangers The refrigerated liquid output from the liquid outlet 12 of the evaporative cooling unit is subjected to secondary cooling, so that the refrigerated liquid is cooled to the target temperature faster, which greatly improves the heat exchange efficiency of the evaporative cooling unit, and finally achieves the improvement of the evaporative cooling system of the utility model. The purpose of the overall heat exchange efficiency of the chiller.
第二个区别点是:本优选结构还包括冷冻液循环泵8,冷冻液循环泵的入口81管道连通所述第一个第二换热器2的冷冻液管道出口22,冷冻液循环泵的出口82管道连通所述进液口A,从而使所制得的低温冷冻液分成两路,一路流向第二个第二换热器2以作二次冷却,另一路则能够重新注入到蒸发式冷却单元内,进一步降低进液口A处的冷冻液温度,使两个第一换热器1内的冷冻液需要分别向两个第一换热器1周围的空气吸收更多热量才能升高温度,以达到进一步降低两个第一换热器1周围空气温度的目的,而当这部分空气被抽风机4抽入到壳体3内部时,则可加快其对喷淋出来的冷却液的冷却作用,最终进一步加快两个第二换热器2内的冷冻液的冷却速度,更进一步地提高了蒸发式冷却单元的换热效率,最终达到进一步提高本实用新型蒸发冷却式冷水机组整体换热效率的目的。The second point of difference is: this preferred structure also includes a cooling liquid circulation pump 8, the inlet 81 of the cooling liquid circulation pump is connected to the cooling liquid pipeline outlet 22 of the first second heat exchanger 2, and the cooling liquid circulation pump The outlet 82 pipe is connected to the liquid inlet A, so that the prepared low-temperature freezing liquid is divided into two paths, one path flows to the second second heat exchanger 2 for secondary cooling, and the other path can be re-injected into the evaporative In the cooling unit, further reduce the temperature of the refrigerant at the liquid inlet A, so that the refrigerant in the two first heat exchangers 1 needs to absorb more heat from the air around the two first heat exchangers 1 to increase temperature, so as to further reduce the temperature of the air around the two first heat exchangers 1, and when this part of the air is sucked into the housing 3 by the exhaust fan 4, it can speed up the spraying of the cooling liquid. The cooling effect finally further accelerates the cooling speed of the refrigerated liquid in the two second heat exchangers 2, further improves the heat exchange efficiency of the evaporative cooling unit, and finally achieves further improving the overall exchange rate of the evaporative cooling water chiller of the utility model. purpose of thermal efficiency.
上述实施方式仅为本实用新型的优选实施方式,不能以此来限定本实用新型保护的范围,本领域的技术人员在本实用新型的基础上所做的任何非实质性的变化及替换均属于本实用新型所要求保护的范围。The above-mentioned embodiments are only preferred embodiments of the present utility model, and cannot be used to limit the scope of protection of the present utility model. The scope of protection required by the utility model.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106322593A (en) * | 2015-07-03 | 2017-01-11 | 广州市华德工业有限公司 | Evaporative cooling type water chilling unit |
| CN108211395A (en) * | 2018-02-08 | 2018-06-29 | 常州瑞持机械有限公司 | For the intelligent MVR vapo(u)rization systems of fermentation |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106322593A (en) * | 2015-07-03 | 2017-01-11 | 广州市华德工业有限公司 | Evaporative cooling type water chilling unit |
| CN106322593B (en) * | 2015-07-03 | 2022-11-15 | 广州市华德工业有限公司 | Evaporative cooling type water chilling unit |
| CN108211395A (en) * | 2018-02-08 | 2018-06-29 | 常州瑞持机械有限公司 | For the intelligent MVR vapo(u)rization systems of fermentation |
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