CN111947489A - Supercooling device with high supercooling efficiency and heat exchanger - Google Patents
Supercooling device with high supercooling efficiency and heat exchanger Download PDFInfo
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- CN111947489A CN111947489A CN202010865354.8A CN202010865354A CN111947489A CN 111947489 A CN111947489 A CN 111947489A CN 202010865354 A CN202010865354 A CN 202010865354A CN 111947489 A CN111947489 A CN 111947489A
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- 238000004781 supercooling Methods 0.000 title claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 50
- 239000003507 refrigerant Substances 0.000 claims abstract description 46
- 230000005494 condensation Effects 0.000 claims abstract description 6
- 238000009833 condensation Methods 0.000 claims abstract description 6
- 239000000498 cooling water Substances 0.000 claims abstract description 6
- 238000001816 cooling Methods 0.000 claims abstract description 5
- 230000007246 mechanism Effects 0.000 claims description 19
- 230000002093 peripheral effect Effects 0.000 claims description 6
- 238000000034 method Methods 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 3
- 238000013021 overheating Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 5
- 238000005192 partition Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 238000000265 homogenisation Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000011555 saturated liquid Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/1615—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium
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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
- F25B39/00—Evaporators; Condensers
- F25B39/04—Condensers
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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
- F25B40/00—Subcoolers, desuperheaters or superheaters
- F25B40/02—Subcoolers
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- Thermal Sciences (AREA)
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- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本发明提供一种过冷效率高的过冷装置及换热器。过冷装置包括:壳体,所述壳体上设置有节流孔和出液口;换热管,设置于所述壳体内部,且所述换热管的两端均贯穿所述壳体与所述液态冷媒连通;液态冷媒由所述节流孔闪发后进入所述壳体与所述换热管进行热交换,并由所述出液口流出所述壳体。本发明提供的过冷效率高的过冷装置及换热器,设置节流孔对液态冷媒进行闪发,利用冷却水对闪发产生的气态冷媒进行冷凝使得闪发过程持续进行,从而增加过冷度,设置均气结构增加气态冷媒与换热管的接触效率,从而有效的提高过冷器内部的换热面积利用率,提高气态冷媒凝结效率。
The invention provides a subcooling device and a heat exchanger with high subcooling efficiency. The subcooling device includes: a casing, which is provided with an orifice and a liquid outlet; a heat exchange tube, which is arranged inside the casing, and both ends of the heat exchange tube pass through the casing The liquid refrigerant is in communication with the liquid refrigerant; the liquid refrigerant flashes from the orifice and enters the casing to exchange heat with the heat exchange tube, and flows out of the casing through the liquid outlet. In the supercooling device and heat exchanger with high supercooling efficiency provided by the present invention, an orifice is arranged to flash liquid refrigerant, and cooling water is used to condense the gaseous refrigerant produced by flashing, so that the flashing process continues, thereby increasing the overheating process. The cooling degree is set, and the air-homogeneous structure is set to increase the contact efficiency between the gaseous refrigerant and the heat exchange tube, thereby effectively improving the utilization rate of the heat exchange area inside the subcooler and improving the condensation efficiency of the gaseous refrigerant.
Description
技术领域technical field
本发明涉及空气处理设备技术领域,特别是一种过冷效率高的过冷装置及换热器。The invention relates to the technical field of air treatment equipment, in particular to a subcooling device and a heat exchanger with high subcooling efficiency.
背景技术Background technique
大型冷水机组空调系统常用管壳式冷凝器,其进口高温过热气态冷媒与换热管内冷却介质进行换热,经冷却、凝结后变为饱和液态冷媒,饱和液态冷媒进入过冷装置进一步降低温度(也即提升其过冷度),最后经过节流进入蒸发器与冷冻水换热,降低冷冻水温度供给用户。过冷装置按照安装形式可分为外置及内置,相比于外置的独立过冷装置,将过冷装置内置于冷凝器内部,可减少系统管路降低泄漏隐患,但常规的内置过冷装置一般采用折流形式进行过冷,结构简单,且受制于冷凝器预留内部空间小,对流换热面积有限,过冷度提升亦是有限。Shell-and-tube condensers are commonly used in large-scale chiller air-conditioning systems. The inlet high-temperature superheated gaseous refrigerant exchanges heat with the cooling medium in the heat exchange tube. After cooling and condensation, it becomes a saturated liquid refrigerant, and the saturated liquid refrigerant enters the subcooling device to further reduce the temperature ( That is to increase its subcooling degree), and finally enter the evaporator through throttling to exchange heat with the chilled water, reduce the temperature of the chilled water and supply it to the user. The subcooling device can be divided into external and built-in according to the installation form. Compared with the external independent subcooling device, the subcooling device is built into the condenser, which can reduce the leakage of the system pipeline and reduce the hidden danger, but the conventional built-in subcooling device The device generally adopts the form of baffle for subcooling, the structure is simple, and due to the small reserved internal space of the condenser, the convection heat exchange area is limited, and the subcooling degree improvement is also limited.
发明内容SUMMARY OF THE INVENTION
为了解决现有技术中折流形式过冷效果差的技术问题,而提供一种在壳体上设置节流孔和换热管进行过冷的过冷效率高的过冷装置及换热器。In order to solve the technical problem of poor subcooling effect of the baffle form in the prior art, a subcooling device and a heat exchanger with high subcooling efficiency are provided in which an orifice and a heat exchange tube are arranged on the casing for subcooling.
一种过冷装置,浸没于液态冷媒内,所述过冷装置包括:A supercooling device immersed in a liquid refrigerant, the supercooling device comprising:
壳体,所述壳体上设置有节流孔和出液口;a casing, which is provided with an orifice and a liquid outlet;
换热管,设置于所述壳体内部,且所述换热管的两端均贯穿所述壳体与冷却水连通;a heat exchange tube, which is arranged inside the shell, and both ends of the heat exchange tube penetrate through the shell to communicate with cooling water;
液态冷媒由所述节流孔闪发后进入所述壳体与所述换热管进行热交换,并由所述出液口流出所述壳体。The liquid refrigerant is flashed from the orifice and then enters the casing for heat exchange with the heat exchange tube, and flows out of the casing through the liquid outlet.
沿所述壳体的长度方向,所述壳体具有相对的第一侧面和第二侧面,所述换热管的一端贯穿所述第一侧面,所述换热管的另一端贯穿所述第二侧面。Along the length direction of the casing, the casing has a first side surface and a second side surface opposite to each other, one end of the heat exchange tube penetrates the first side surface, and the other end of the heat exchange tube penetrates the first side surface. Two sides.
所述第一侧面上设置有所述节流孔;或所述第二侧面上设置有所述节流孔;或所述第一侧面上和所述第二侧面上均设置有所述节流孔。The throttle hole is provided on the first side surface; or the throttle hole is provided on the second side surface; or the throttle hole is provided on both the first side surface and the second side surface hole.
所述换热管的数量为多个,且所述换热管的端部均匀分布于所述节流孔的周侧。The number of the heat exchange tubes is plural, and the ends of the heat exchange tubes are evenly distributed on the peripheral side of the orifice.
所述过冷装置还包括均气机构,所述均气机构设置于所述壳体内部,且所述节流孔通过所述均气机构与所述壳体的内部连通。The supercooling device further includes an air equalizing mechanism, the air equalizing mechanism is arranged inside the casing, and the throttle hole communicates with the inside of the casing through the air equalizing mechanism.
所述均气机构为管状结构,所述管状结构的端部抵接于所述壳体的内表面上,且所述管状结构的端部与所述节流孔连通,所述管状结构的周侧面上设置有均气孔。The air equalizing mechanism is a tubular structure, the end of the tubular structure abuts on the inner surface of the casing, and the end of the tubular structure communicates with the throttle hole, and the circumference of the tubular structure is in contact with the orifice. There are even air holes on the side.
所述管状结构的截面为圆形或方形。The cross section of the tubular structure is circular or square.
所述管状结构包括依次连接的五个平面,相邻两个所述平面之间均具有夹角,且五个所述平面上均设置有均气孔。The tubular structure includes five planes connected in sequence, two adjacent planes each have an included angle, and all five planes are provided with uniform air holes.
五个所述平面包括依次连接的第一平面、第二平面、第三平面、第四平面和第五平面,所述第五平面与所述壳体的底面平行,且所述第一平面、第二平面、第三平面和第四平面均设置于所述第五平面远离所述底面的一侧。The five planes include a first plane, a second plane, a third plane, a fourth plane and a fifth plane that are connected in sequence, the fifth plane is parallel to the bottom surface of the casing, and the first plane, The second plane, the third plane and the fourth plane are all disposed on the side of the fifth plane away from the bottom surface.
所述节流孔的截面为圆形或方形。The cross section of the orifice is circular or square.
一种换热器,包括上述的过冷装置。A heat exchanger, comprising the above-mentioned subcooling device.
所述过冷装置处于所述换热器内部的液面以下;或所述节流孔处于所述换热器内部的液面以下。The subcooling device is below the liquid level inside the heat exchanger; or the orifice is below the liquid level inside the heat exchanger.
所述换热器内设置有支撑板,所述支撑板上形成有换热管孔,且所述支撑板的边沿与所述壳体固定设置。A support plate is arranged in the heat exchanger, a heat exchange tube hole is formed on the support plate, and the edge of the support plate is fixedly arranged with the casing.
所述换热器内设置有隔板,所述隔板将所述换热器分为冷凝区域和过冷区域,所述过冷装置设置于所述过冷区域内。The heat exchanger is provided with a partition, the partition divides the heat exchanger into a condensation area and a subcooling area, and the subcooling device is arranged in the subcooling area.
本发明提供的过冷效率高的过冷装置及换热器,设置节流孔对液态冷媒进行闪发过冷,利用冷却水对闪发产生的气态冷媒进行冷凝使得闪发过程持续进行,从而增加过冷度,设置均气结构增加气态冷媒与换热管的接触效率,从而有效的提高过冷器内部的换热面积利用率,提高气态冷媒凝结效率。In the subcooling device and heat exchanger with high subcooling efficiency provided by the present invention, an orifice is arranged to flash and supercool the liquid refrigerant, and cooling water is used to condense the gaseous refrigerant produced by the flash, so that the flash process continues, thereby Increase the degree of subcooling, and set up a gas-equalizing structure to increase the contact efficiency between the gaseous refrigerant and the heat exchange tube, thereby effectively improving the utilization rate of the heat exchange area inside the subcooler and improving the condensation efficiency of the gaseous refrigerant.
附图说明Description of drawings
图1为本发明提供的过冷效率高的过冷装置及换热器的实施例的换热器的结构示意图;1 is a schematic structural diagram of a heat exchanger according to an embodiment of a subcooling device with high subcooling efficiency and a heat exchanger provided by the present invention;
图2为本发明提供的过冷效率高的过冷装置及换热器的实施例的过冷装置的结构示意图;2 is a schematic structural diagram of a subcooling device of an embodiment of a subcooling device with high subcooling efficiency and a heat exchanger provided by the present invention;
图3为本发明提供的过冷效率高的过冷装置及换热器的实施例的过冷装置的侧视图;3 is a side view of the subcooling device of the embodiment of the subcooling device with high subcooling efficiency and the heat exchanger provided by the present invention;
图4为本发明提供的过冷效率高的过冷装置及换热器的实施例的过冷装置的侧剖视图;4 is a side cross-sectional view of the subcooling device of the embodiment of the subcooling device with high subcooling efficiency and the heat exchanger provided by the present invention;
图5为本发明提供的过冷效率高的过冷装置及换热器的实施例的过冷装置的透视图;5 is a perspective view of a subcooling device of an embodiment of a subcooling device with high subcooling efficiency and a heat exchanger provided by the present invention;
图6为本发明提供的过冷效率高的过冷装置及换热器的实施例的均液机构的结构示意图;6 is a schematic structural diagram of the liquid homogenization mechanism of the embodiment of the subcooling device with high subcooling efficiency and the heat exchanger provided by the present invention;
图中:In the picture:
1、壳体;11、节流孔;12、出液口;2、换热管;3、均气机构;31、均气孔。1. Shell; 11. Orifice; 12. Liquid outlet; 2. Heat exchange tube; 3. Air equalization mechanism; 31. Air equalization hole.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合附图及实施例对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅用于解释本发明,并不用于限定本发明。In order to make the objectives, technical solutions and advantages of the present invention clearer, the present invention will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are only used to explain the present invention, but not to limit the present invention.
如图1至图6所示的过冷装置,浸没于液态冷媒内,所述过冷装置包括:壳体1,所述壳体1上设置有节流孔11和出液口12,所述壳体1的内部与所述壳体1的外部相对密封,从而使壳体1内部的冷媒与壳体1外部的冷媒之间不会相互流动,而壳体1外部的冷媒只能从节流孔11流入至壳体1的内部,从而必须要经过节流孔11的节流闪发作用进行一次过冷,而出液口12是用于将壳体1内部的液态冷媒(包括过冷部分和直接从节流孔11流入的部分)排出壳体1;换热管2,设置于所述壳体1内部,且所述换热管2的两端均贯穿所述壳体1与冷却水连通,换热管2将冷却水引入壳体1内部,与壳体1内部的气态冷媒进行换热,从而将闪发后的气态冷媒进行冷凝形成液态过冷冷媒,实现二次过冷;液态冷媒由所述节流孔11闪发后分为气态冷媒和液态冷媒,液态冷媒直接由出液口12排出壳体1,而气态冷媒进入所述壳体1后与换热管2进行热交换,冷凝成过冷液态冷媒,并由所述出液口12流出所述壳体1,从而整个过冷装置能够实现对冷媒的二次过冷增加过冷效率。The subcooling device shown in Figures 1 to 6 is immersed in a liquid refrigerant. The subcooling device includes: a
沿所述壳体1的长度方向,所述壳体1具有相对的第一侧面和第二侧面,所述换热管2的一端贯穿所述第一侧面,所述换热管2的另一端贯穿所述第二侧面,也即液态冷媒能够从壳体1的长度方向的一侧进入所述壳体1并由壳体1的另一侧流出完成流动。Along the length direction of the
所述第一侧面上设置有所述节流孔11;或所述第二侧面上设置有所述节流孔11;或所述第一侧面上和所述第二侧面上均设置有所述节流孔11,根据壳体1的设置位置选择节流孔11的位置。The
所述换热管2的数量为多个,且所述换热管2的端部均匀分布于所述节流孔11的周侧,从而使从节流孔11流出的气态冷媒能够在任意方向上均能够与换热管2进行接触换热,保证过冷效果。The number of the
所述过冷装置还包括均气机构3,所述均气机构3设置于所述壳体1内部,且所述节流孔11通过所述均气机构3与所述壳体1的内部连通,将节流孔11闪发出的气态冷媒通过均气机构3进行均匀分配,从而使换热管2能够进行均匀换热,增加过冷效果。The subcooling device further includes an air equalizing
所述均气机构3为管状结构,所述管状结构的端部抵接于所述壳体1的内表面上,且所述管状结构的端部与所述节流孔11连通,所述管状结构的周侧面上设置有均气孔31,从而使管状结构能够将气态冷媒送至位于所述节流孔11周侧的换热管2上进行换热,增加气态冷媒的换热效率进而提高过冷效率。The
所述管状结构的截面为圆形或方形。The cross section of the tubular structure is circular or square.
所述管状结构包括依次连接的五个平面,相邻两个所述平面之间均具有夹角,且五个所述平面上均设置有均气孔31。The tubular structure includes five planes connected in sequence, two adjacent planes each have an included angle, and each of the five planes is provided with air holes 31 .
五个所述平面包括依次连接的第一平面、第二平面、第三平面、第四平面和第五平面,所述第五平面与所述壳体1的底面平行,且所述第一平面、第二平面、第三平面和第四平面均设置于所述第五平面远离所述底面的一侧,第一平面为A,第二平面为B,第三平面为C,第四平面为D,第五平面为E,其中A、B、C、D为倾斜出气面,底部E面为水平出液面,也即气态冷媒经过多孔均气后由A、B、C、D四面流向外侧的传热管、保证在适当的流速下与各个换热管进行充分接触。A、B、C、D面均为倾斜布置,且交错开孔,换热管正对均气机构的开孔进行布管,冷媒气体垂直流向换热管,凝结下来的液态冷媒受重力向下滴落,A、B面多孔板倾斜布置可使得其上部凝结夜顺利向下流动至壳体底部或者经过小孔进入均气机构内部,再经过E面小孔流出至壳体底部。C、D面流出的气体凝结后,直接在重力作用下滴入壳体底部,避免气体涌向局部区域不能充分利用换热换热面积,开孔大小及数量根据闪发量及循环量有关,保证合适的气流速度与换热管接触,提高换热效率。均气机构的E面装配在底部,其上也开设有孔或缝,使得进入均气机构内部的液体能够顺利流出至壳体底部,并最终流出壳体1。The five planes include a first plane, a second plane, a third plane, a fourth plane and a fifth plane connected in sequence, the fifth plane is parallel to the bottom surface of the
所述节流孔11的截面为圆形或方形。The cross section of the
一种换热器,包括上述的过冷装置。A heat exchanger, comprising the above-mentioned subcooling device.
所述过冷装置处于所述换热器内部的液面以下;或所述节流孔11处于所述换热器内部的液面以下,从而使换热器内的液态冷媒能够进入过冷装置内部进行过冷。The subcooling device is below the liquid level inside the heat exchanger; or the
所述换热器内设置有支撑板,所述支撑板上形成有换热管孔,且所述支撑板的边沿与所述壳体1固定设置,也即将换热器内的支撑板与壳体1进行固定,保证壳体1固定的可靠性。The heat exchanger is provided with a support plate, a heat exchange tube hole is formed on the support plate, and the edge of the support plate is fixedly arranged with the
所述换热器内设置有隔板,所述隔板将所述换热器分为冷凝区域和过冷区域,所述过冷装置设置于所述过冷区域内。The heat exchanger is provided with a partition, the partition divides the heat exchanger into a condensation area and a subcooling area, and the subcooling device is arranged in the subcooling area.
所述换热器设置有出液管,所述出液口12与所述出液管连通,使进入所述过冷装置内部的冷媒流动到壳体1的底部后,由所述出液口12直接输送至出液管内,而保证壳体1内部的冷媒能够顺利的通过出液口12流出,避免换热器内部的液态冷媒从所述出液口12进入所述壳体而影响过冷装置的过冷效果,也能够避免出液口12流出的液态冷媒需要克服换热器内部的压力而造成出液不畅的问题。The heat exchanger is provided with a liquid outlet pipe, and the
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。因此,本发明专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only represent several embodiments of the present invention, and the descriptions thereof are specific and detailed, but should not be construed as limiting the scope of the patent of the present invention. It should be noted that, for those skilled in the art, without departing from the concept of the present invention, several modifications and improvements can be made, which all belong to the protection scope of the present invention. Therefore, the protection scope of the patent of the present invention should be subject to the appended claims.
Claims (14)
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| CN202010865354.8A CN111947489A (en) | 2020-08-25 | 2020-08-25 | Supercooling device with high supercooling efficiency and heat exchanger |
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