CN201858821U - A refrigerant evaporative cooler - Google Patents
A refrigerant evaporative cooler Download PDFInfo
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- CN201858821U CN201858821U CN2010205141126U CN201020514112U CN201858821U CN 201858821 U CN201858821 U CN 201858821U CN 2010205141126 U CN2010205141126 U CN 2010205141126U CN 201020514112 U CN201020514112 U CN 201020514112U CN 201858821 U CN201858821 U CN 201858821U
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- 239000003507 refrigerant Substances 0.000 title claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 238000009833 condensation Methods 0.000 claims abstract description 18
- 230000005494 condensation Effects 0.000 claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 12
- 238000005507 spraying Methods 0.000 claims abstract 2
- 239000007788 liquid Substances 0.000 claims description 11
- 230000017525 heat dissipation Effects 0.000 claims description 8
- 238000003491 array Methods 0.000 claims description 3
- 239000002184 metal Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 238000007710 freezing Methods 0.000 abstract description 3
- 230000008014 freezing Effects 0.000 abstract description 3
- 230000001502 supplementing effect Effects 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 7
- 239000007921 spray Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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Abstract
Description
【技术领域】【Technical field】
本实用新型涉及制冷设备,具体地说是一种制冷剂蒸发冷却器。The utility model relates to refrigeration equipment, in particular to a refrigerant evaporation cooler.
【背景技术】【Background technique】
在制冷装置中,冷凝器种类很多,通常有风冷式冷凝器,带冷却水塔或不带冷却水塔的水冷式冷凝器及蒸发式冷凝器,风冷式冷凝器存在运行效率低,系统运行费用相对较高,体积庞大,噪音高及较高压缩比导致的压缩机使用寿命缩短等缺陷,冷热两用是其最大优势。水冷式冷凝器运行效率较高、结构紧凑,但主机运行必需配置冷却水塔及冷却水循环系统,耗水量大且需要增加水处理费用,主机运行仅能实现单一制冷功能。蒸发式冷凝器是一种融合了风冷式、水冷式和冷却塔的紧凑型换热设备,主要依靠水份的蒸发使制冷剂冷凝散热,运行效率最高。In refrigeration devices, there are many types of condensers, usually air-cooled condensers, water-cooled condensers with or without cooling water towers, and evaporative condensers. Air-cooled condensers have low operating efficiency and system operating costs Relatively high, bulky, high noise and shortened service life of the compressor due to high compression ratio, etc., the dual use of cooling and heating is its biggest advantage. The water-cooled condenser has high operating efficiency and compact structure, but the main engine must be equipped with a cooling tower and a cooling water circulation system, which consumes a lot of water and requires additional water treatment costs. The main engine can only achieve a single cooling function. The evaporative condenser is a compact heat exchange equipment that combines air-cooled, water-cooled and cooling towers. It mainly relies on the evaporation of water to condense the refrigerant to dissipate heat, and has the highest operating efficiency.
目前,传统蒸发式冷凝器结构型式通常分为异形管式(包括有圆管、椭圆管、异滴形管、锥形圆弧管和交变扭曲管等)、蒸发式冷凝器和板式或板管式蒸发式冷凝器,它们均存在如下方面的不足:1、传热元件为光管束或平面板束,有效换热面积小,管束或板片外侧传热系数低,设备体积庞大;2、需额外增加PVC填料热交换层,PVC填料易积灰、积垢且易腐烂变性,需要经常更换;3、由于冷凝器有效换热面积小,因此在在系统冷凝负荷较低或外界环境温度较低时,仍需开启水泵才能保证设备运行,冬季存在冻结的危险;4、过渡季节或冬季无法实现正常制热运行;5、制冷剂蒸汽直接进入蒸发式冷凝器进行相变换热,传热管或板表面喷淋水温度较高,冷凝器表面易结垢。At present, the traditional evaporative condenser structure is usually divided into special-shaped tube type (including round tube, oval tube, different drop-shaped tube, conical arc tube and alternating twisted tube, etc.), evaporative condenser and plate or plate Tubular evaporative condensers all have the following deficiencies: 1. The heat transfer element is a bare tube bundle or a flat plate bundle, the effective heat exchange area is small, the heat transfer coefficient outside the tube bundle or plate is low, and the equipment is bulky; 2. It is necessary to add an additional heat exchange layer of PVC filler. PVC filler is easy to accumulate dust, scale and rot and denature, so it needs to be replaced frequently; When the temperature is low, the water pump still needs to be turned on to ensure the operation of the equipment, and there is a danger of freezing in winter; 4. Normal heating operation cannot be realized in transitional seasons or winter; 5. Refrigerant steam directly enters the evaporative condenser for phase-change heat transfer. The temperature of the spray water on the surface of the tube or plate is high, and the surface of the condenser is easy to scale.
因此,本实用新型针对现有技术不足,对蒸发式冷凝器作进一步改进。Therefore, the utility model further improves the evaporative condenser aiming at the deficiencies of the prior art.
【实用新型内容】【Content of utility model】
本实用新型的目的在于提供一种具有传热效率高,结构更加紧凑,制冷剂充注量少,不易形成垢层,抗腐蚀能力强及长期运行效率稳定的制冷剂蒸发冷却器。The purpose of the utility model is to provide a refrigerant evaporative cooler with high heat transfer efficiency, more compact structure, less refrigerant charge, less scale formation, strong corrosion resistance and stable long-term operating efficiency.
为达到上述目的,本实用新型采用以下技术方案:In order to achieve the above object, the utility model adopts the following technical solutions:
一种制冷剂蒸发冷却器,包括有箱体、过热蒸汽冷却器,热交换器、集水箱、循环水泵、风机、喷淋装置以及补水装置,所述过热蒸汽冷却器与热交换器相连接,其特征在于所述热交换器包括有集气管、集液管及冷凝盘管,所述冷凝盘管的进气端口分别与集气管相连通,所述冷凝盘管的出液端口分别与集液管相连通,所述冷凝盘管是由传热管及散热肋片构成。A refrigerant evaporative cooler, including a box body, a superheated steam cooler, a heat exchanger, a water collection tank, a circulating water pump, a fan, a spray device and a water supply device, the superheated steam cooler is connected with the heat exchanger, It is characterized in that the heat exchanger includes a gas collection pipe, a liquid collection pipe and a condensation coil, the inlet ports of the condensation coil are respectively connected with the gas collection pipe, and the liquid outlet ports of the condensation coil are connected with the liquid collection pipe respectively. The tubes are connected, and the condensation coil is composed of heat transfer tubes and cooling fins.
如上所述的一种制冷剂蒸发冷却器,其特征在于所述过热蒸汽冷却器包括有进气管及出气管及预冷凝盘管,所述预冷凝盘管的前端与进气管相连通,所述预冷凝盘管的后端与出气管相连通;所述出气管与热交换器的集气管相连通;所述预冷凝盘管由传热管及肋片构成。A refrigerant evaporative cooler as described above is characterized in that the superheated steam cooler includes an inlet pipe, an outlet pipe and a pre-condensation coil, the front end of the pre-condensation coil is connected to the inlet pipe, and the The rear end of the pre-condensing coil is connected with the air outlet pipe; the air outlet pipe is connected with the gas collecting pipe of the heat exchanger; the pre-condensing coil is composed of heat transfer tubes and fins.
如上所述的一种制冷剂蒸发冷却器,其特征在于所述冷凝盘管和预冷凝盘管为多个阵列分布。A refrigerant evaporative cooler as described above is characterized in that the condensing coils and the pre-condensing coils are distributed in multiple arrays.
如上所述的一种制冷剂蒸发冷却器,其特征在于所述散热肋片呈螺旋形状分布或呈独立片状排列分布。A refrigerant evaporative cooler as described above is characterized in that the heat dissipation fins are distributed in a spiral shape or arranged in an independent sheet shape.
如上所述的一种制冷剂蒸发冷却器,其特征在于所述散热肋片卡在传热管上或者套在传热管上。A refrigerant evaporative cooler as described above is characterized in that the heat dissipation fins are clamped on or sleeved on the heat transfer tubes.
如上所述的一种制冷剂蒸发冷却器,其特征在于在箱体的侧面进风口处设有空气过滤器。A refrigerant evaporative cooler as described above is characterized in that an air filter is provided at the side air inlet of the box body.
如上所述的一种制冷剂蒸发冷却器,其特征在于在箱体的左右两侧分别设有热交换器,所述热交换器之间设有挡水板。A refrigerant evaporative cooler as described above is characterized in that heat exchangers are respectively arranged on the left and right sides of the box body, and water baffles are arranged between the heat exchangers.
本实用新型的有益效果有:1、由于在冷凝盘管上设置金属肋片,增加了热交换面积,有利于提高传热效率;2、结构更加紧凑,制冷剂充注量更少,有利于降低成本;3、在系统冷凝负荷较低或外界环境温度较低时,可采用风直接冷却,解决了冬季的冻结问题;4、冷凝盘管有效换热面积增加明显,因此设备可实现过渡季节或冬季的正常制热运行。The beneficial effects of the utility model are as follows: 1. Since the metal fins are arranged on the condensing coil, the heat exchange area is increased, which is conducive to improving the heat transfer efficiency; 2. The structure is more compact, and the refrigerant charge is less, which is beneficial to Reduce costs; 3. When the system condensing load is low or the external environment temperature is low, direct wind cooling can be used to solve the freezing problem in winter; 4. The effective heat exchange area of the condensing coil increases significantly, so the equipment can realize the transition season Or normal heating operation in winter.
【附图说明】【Description of drawings】
下面结合附图与实施例对本实用新型作详细说明;Below in conjunction with accompanying drawing and embodiment the utility model is described in detail;
图1是本实用新型结构布置示意图;Fig. 1 is a schematic diagram of the structural layout of the utility model;
图2是本实用新型热交换器结构示意图;Fig. 2 is a structural schematic diagram of the utility model heat exchanger;
图3是图2的左视图;Fig. 3 is the left view of Fig. 2;
图4是图2的俯视图;Fig. 4 is the top view of Fig. 2;
图5是本实用新型过热蒸汽冷却器2结构示意图;Fig. 5 is a structural schematic diagram of the utility model superheated
图6是图5的左视图;Fig. 6 is the left side view of Fig. 5;
图7是图5的俯视图;Figure 7 is a top view of Figure 5;
图8是冷凝盘管示意图;Fig. 8 is a schematic diagram of a condensing coil;
图9是本实用新型肋片安装结构示意图一;Fig. 9 is a schematic diagram of a rib installation structure of the present invention;
图10是本实用新型肋片安装结构示意图二;Fig. 10 is a second schematic diagram of the rib installation structure of the utility model;
图11是本实用新型肋片安装结构示意图三;Fig. 11 is the third schematic diagram of the rib installation structure of the utility model;
【具体实施方式】【Detailed ways】
如图1所示,本实用新型所指的一种制冷剂蒸发冷却器,包括有箱体1、过热蒸汽冷却器2,热交换器3、集水箱4、循环水泵5、风机6、喷淋装置7以及补水装置8,所述过热蒸汽冷却器2与热交换器3相连接。所述集水箱4设置在热交换器3的下方,所述喷淋装置7设置在热交换器3的上方。所述循环水泵5一端通过管道与集水箱4相连接,另一端通过管道连接喷淋装置7。所述风机6设置在箱体1的顶部,位于过热蒸汽冷却器2的正上方。其中所述热交换器3包括有集气管9、集液管10及冷凝盘管11,所述冷凝盘管11的进气端口分别与集气管9相连通,所述冷凝盘管11的出液端口分别与集液管10相连通,所述冷凝盘管11是由传热管12及散热肋片13构成。As shown in Figure 1, a refrigerant evaporative cooler referred to in the utility model includes a box body 1, a
本实用新型中,所述过热蒸汽冷却器2包括有进气管14及出气管15及预冷凝盘管16,所述预冷凝盘管16的前端与进气管14相连通,所述预冷凝盘管16的后端与出气管15相连通;所述出气管15与热交换器3的集气管9相连通;所述预冷凝盘管16由传热管17及肋片18构成。In the utility model, the
在本实施例中,所述冷凝盘管11和预冷凝盘管16为多个阵列分布。所述散热肋片13、18呈螺旋形状分布或呈独立片状排列分布。所述散热肋片13、18卡在传热管12、17上或者套在传热管12、17上。In this embodiment, the
并在箱体1的侧面进风口处设有空气过滤器19。为了使冷却效果更好,在箱体1的左右两侧分别设有热交换器3,所述热交换器3之间设有挡水板20。And an
本实用新型的原理是:高温高压的制冷剂蒸汽经先经过热蒸汽冷却器进行预冷却,再将预冷却后的制冷剂蒸汽经出气管输入热交换器进行二次冷却,经过二次冷却作用,制冷剂从气态变成液态,此时转变成低温高压的制冷剂液体再流出冷却器外。The principle of the utility model is: the high-temperature and high-pressure refrigerant steam is pre-cooled through the hot steam cooler, and then the pre-cooled refrigerant steam is input into the heat exchanger through the outlet pipe for secondary cooling. , the refrigerant changes from a gaseous state to a liquid state, and at this time it turns into a low-temperature and high-pressure refrigerant liquid and then flows out of the cooler.
本实用新型通过循环水泵5将集水箱4中的水抽出,并由喷淋装置5将水喷洒在热交换器3上,由于热交换器3采用冷凝盘管11结构,并在冷凝盘管11上设置金属散热肋片13,使冷凝盘管11的热交换面积大增,更有利于制冷剂的热质交换,使冷却效果更好。在过热蒸汽冷却器2内设置预冷凝盘管16,并在预冷凝盘管16上设置金属散热肋片13,一方面可有效防止冷凝盘管11的高温段在经喷啉水后形成结垢,并进一步提搞传热效率达10%左右,节能效果更加明显。The utility model extracts the water in the water collecting
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102305445A (en) * | 2011-08-26 | 2012-01-04 | 西安工程大学 | Gravity type heat pipe and direct evaporation cooler compound evaporating and cooling water chilling unit |
CN102393152A (en) * | 2011-12-01 | 2012-03-28 | 上海宝丰机械制造有限公司 | Finned mixed flow type evaporative condenser and condensing coil thereof |
CN103123189A (en) * | 2013-02-06 | 2013-05-29 | 刘玉岭 | Evaporative-type condenser and heat source device of the same |
CN104964475A (en) * | 2015-07-10 | 2015-10-07 | 广东欧科空调制冷有限公司 | Composite evaporation cooling type heat pump unit |
CN104990316A (en) * | 2015-07-31 | 2015-10-21 | 华南理工大学 | Superheat section and condensing section-separately arranged evaporation type condensation heat exchanger and method thereof |
CN110985209A (en) * | 2019-10-30 | 2020-04-10 | 北京动力机械研究所 | High-compactness large-heat-capacity-ratio-difference heat exchanger structure and manufacturing process thereof |
-
2010
- 2010-08-27 CN CN2010205141126U patent/CN201858821U/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102305445A (en) * | 2011-08-26 | 2012-01-04 | 西安工程大学 | Gravity type heat pipe and direct evaporation cooler compound evaporating and cooling water chilling unit |
CN102393152A (en) * | 2011-12-01 | 2012-03-28 | 上海宝丰机械制造有限公司 | Finned mixed flow type evaporative condenser and condensing coil thereof |
CN102393152B (en) * | 2011-12-01 | 2013-04-24 | 上海宝丰机械制造有限公司 | Finned mixed flow type evaporative condenser and condensing coil thereof |
CN103123189A (en) * | 2013-02-06 | 2013-05-29 | 刘玉岭 | Evaporative-type condenser and heat source device of the same |
CN104964475A (en) * | 2015-07-10 | 2015-10-07 | 广东欧科空调制冷有限公司 | Composite evaporation cooling type heat pump unit |
CN104990316A (en) * | 2015-07-31 | 2015-10-21 | 华南理工大学 | Superheat section and condensing section-separately arranged evaporation type condensation heat exchanger and method thereof |
CN110985209A (en) * | 2019-10-30 | 2020-04-10 | 北京动力机械研究所 | High-compactness large-heat-capacity-ratio-difference heat exchanger structure and manufacturing process thereof |
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