CN103344135A - Plate type evaporative condenser - Google Patents
Plate type evaporative condenser Download PDFInfo
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- CN103344135A CN103344135A CN2013103049320A CN201310304932A CN103344135A CN 103344135 A CN103344135 A CN 103344135A CN 2013103049320 A CN2013103049320 A CN 2013103049320A CN 201310304932 A CN201310304932 A CN 201310304932A CN 103344135 A CN103344135 A CN 103344135A
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Abstract
Description
技术领域 technical field
本发明涉及一种蒸发式冷凝器,具体涉及一种板式蒸发式冷凝器。 The invention relates to an evaporative condenser, in particular to a plate evaporative condenser. the
背景技术 Background technique
现有的板式蒸发式冷凝器,在壳体内设置一组板壳式散热器,向上或者向下喷淋循环冷却水,冷却水在散热器表面蒸发,在轴流风机作用下带走蒸发水汽,从而带走自上而下流动的散热器管程介质的热能,达到对管程介质的冷凝目的。按照壳体内风向与喷水方向之间的关系可分为逆流式和顺流式两种。其中逆流式由于散热板间隙较小,风带水上行影响水向下运行,并且需要在蒸发冷上部设置足够大的空间挡水,并且传热效果不好。现有的顺流式蒸发冷中,风和水的流动方向均是自下而上,这一方向与管程介质流动方向相反,影响了热交换效率。 In the existing plate-type evaporative condenser, a group of plate-shell radiators are installed in the shell, and circulating cooling water is sprayed upward or downward, and the cooling water evaporates on the surface of the radiator, and the evaporated water vapor is taken away by the axial flow fan In this way, the heat energy of the tube-side medium of the radiator flowing from top to bottom is taken away, and the purpose of condensing the tube-side medium is achieved. According to the relationship between the wind direction in the housing and the water spray direction, it can be divided into two types: counter-flow type and downstream type. Among them, the counterflow type has a small gap between the cooling plates, the wind brings the water up and affects the water running down, and it needs to set up a large enough space on the upper part of the evaporative cooling to block the water, and the heat transfer effect is not good. In the existing down-flow evaporative cooling, the flow direction of wind and water is from bottom to top, which is opposite to the flow direction of the tube-side medium, which affects the heat exchange efficiency. the
发明内容 Contents of the invention
本发明所要解决的技术问题是,提供一种板式蒸发冷凝器,集中逆流式和顺流式蒸发冷的优点,具有更高的热交换效率,以克服已有逆流式和顺流式蒸发冷蒸发效果差的缺陷。 The technical problem to be solved by the present invention is to provide a plate-type evaporative condenser, which combines the advantages of counter-current and forward-flow evaporative cooling, and has higher heat exchange efficiency, so as to overcome the poor evaporation effect of the existing counter-current and forward-current evaporative cooling. Defects. the
本发明的技术方案如下: Technical scheme of the present invention is as follows:
一种板式蒸发冷凝器,包括壳体和集水槽,壳体的上端安装有轴流风机,壳体的内部安装有挡水板,其特征在于: 在挡水板下方安装有至少两块具有导风作用的导向隔板,导向隔板的根部与壳体内壁相连接,导向隔板的悬空端与壳体内壁之间留有风水折流口;相邻两块导向隔板的风水折流口分别位于壳体内相对的两侧;相邻两块导向隔板之间以及最下方导向隔板的下方的壳体腔内各设置有作为板式散热器的一组管板组,每一管板组分别由并列竖排的若干个管板束并联而成;相邻管板组的管板束互相连接形成被冷凝介质通道;被冷凝介质入口设在最上方管板组的上端,出口设在最下方管板组的下端;壳体还带有位于最下方管板组侧面的进风口;在每一管板组的侧面分别安装有一组喷淋水管组,所述喷淋水管组分别所述集水槽相连接。 A plate-type evaporative condenser, including a shell and a water collection tank, an axial flow fan is installed on the upper end of the shell, and a water baffle is installed inside the shell. The guide partition for the wind effect, the root of the guide partition is connected with the inner wall of the shell, and there is a wind-shui deflection opening between the suspended end of the guide partition and the inner wall of the shell; the wind-shui deflection port of two adjacent guide partitions They are respectively located on opposite sides of the housing; a set of tube-sheet groups as plate radiators are respectively arranged between two adjacent guide partitions and in the housing cavity below the lowest guide partition, and each tube-sheet group is respectively It is formed by parallel connection of several tubesheet bundles arranged vertically; the tubesheet bundles of adjacent tubesheet groups are connected to each other to form the condensed medium channel; the condensed medium inlet is set at the upper end of the uppermost tubesheet group, and the outlet is set at the bottom The lower end of the tube plate group; the shell also has an air inlet located on the side of the bottom tube plate group; a group of spray water pipe groups are respectively installed on the side of each tube plate group, and the spray water pipe groups are respectively described in the sump connected.
进风口、喷淋水管组、导向隔板三者的位置设计满足如下条件:每组喷淋水管组的喷水方向与风流向一致,水、汽经过风水折流口时折流运行。 The positions of the air inlet, spray water pipe group and guide partition are designed to meet the following conditions: the water spray direction of each spray water pipe group is consistent with the wind flow direction, and the water and steam are deflected when passing through the wind and water diversion opening. the
优选地,相邻上、下方管板组的管板束之间通过集管相连接。 Preferably, the tubesheet bundles of the adjacent upper and lower tubesheet groups are connected through headers. the
本发明的积极效果在于: The positive effect of the present invention is:
第一、通过导向隔板将壳体内腔分隔为不同温度的至少两个蒸发区,上方蒸发区的温度高于下方蒸发区,排风端的温度高于进风端,因此同流量风带走更多热量,并且下侧进风,上端出风,各组喷水方向均与风向一致,喷淋水在向上的风剪切力和向下的重力作用下能够在管板组表面形成拉膜并且布膜更均匀,更容易使水汽化。本发明集中了逆流式和顺流式蒸发冷的优点同时克服了它们的缺点,具有更好的蒸发效率。 First, the inner cavity of the shell is divided into at least two evaporation areas with different temperatures by the guide partition. The temperature of the upper evaporation area is higher than that of the lower evaporation area, and the temperature of the exhaust end is higher than that of the air intake end. There is a lot of heat, and the lower side enters the wind and the upper end exits the wind. The spraying direction of each group is consistent with the wind direction. The spraying water can form a film on the surface of the tube plate group under the upward wind shear force and downward gravity. The cloth film is more uniform and it is easier to vaporize the water. The present invention integrates the advantages of the counter-flow type and the down-flow type evaporative cooling while overcoming their shortcomings, and has better evaporation efficiency.
第二、随着自上而下运行,被冷凝介质发生相变(冷凝),体积逐渐缩小,本发明通过导向隔板将壳体内腔分隔为不同腔室,能够根据介质相变特性对不同管板组的管板束数量进行调整,使下方管板组的管板束数量小于上方管板组,提高了被冷凝介质的流速,增加了介质的循环频率,进一步提高了热交换效率。 Second, with the operation from top to bottom, the phase change (condensation) of the condensed medium occurs, and the volume gradually shrinks. The present invention divides the inner cavity of the shell into different chambers through the guide partition, and can control different tubes according to the phase change characteristics of the medium. The number of tubesheet bundles in the plate group is adjusted so that the number of tubesheet bundles in the lower tubesheet group is smaller than that in the upper tubesheet group, which increases the flow rate of the condensed medium, increases the circulation frequency of the medium, and further improves the heat exchange efficiency. the
附图说明 Description of drawings
图1是本发明实施例的结构和工作原理示意图。 Fig. 1 is a schematic diagram of the structure and working principle of an embodiment of the present invention. the
图2是本发明实施例一个管板组的侧向形状、结构示意图。 Fig. 2 is a schematic diagram of the lateral shape and structure of a tube-sheet group according to an embodiment of the present invention. the
具体实施方式 Detailed ways
下面结合附图和实施例进一步说明本发明。 The present invention will be further described below in conjunction with the accompanying drawings and examples.
如图1,本实施例包括壳体5,壳体5的上端安装有轴流风机10,下端带有集水槽14,内部安装有挡水板17。在壳体5内挡水板17和集水槽14之间安装有具有导风作用的下导向隔板7和上导向隔板9,下导向隔板7和上导向隔板9的根部均与壳体内壁连接,悬浮端与壳体内壁之间留有风水折流口;下导向隔板7和上导向隔板9的的风水折流口分别位于壳体内相对的左、右两侧。
As shown in Fig. 1 , this embodiment includes a
下导向隔板7和上导向隔板9将壳体内腔分隔为汽水分离、高温蒸发和低温蒸发三个区。
The
在壳体腔内分别安装有位于下导向隔板7和上导向隔板9之间的上管板组8,还安装有位于下导向隔板7下方的下管板组6,每一管板组分别由并列竖排的若干个管板束16并联而成,如图2。上管板组8与下管板组6的管板束互相串联形成被冷凝介质通道。作为被冷凝流体的管程介质入口设在上管板组8的上端,出口设在下管板组6的下端。
The upper
上、下管板束之间具体连接方式包括:上管板组8的管板束分别连接集管11,下管板组6的管板束也分别连接该集管11。
The specific connection methods between the upper and lower tubesheet bundles include: the tubesheet bundles of the
壳体5还带有位于下管板组6侧面的进风口4,进风口4位于上导向隔板9的的风水折流口同一侧壳体上并且位于下导向隔板7下方。在进风口4内侧安装有第一喷淋水管组3,在上管板组8的侧面安装有第二喷淋水管组12,第二喷淋水管组12位于第一喷淋水管组3对面一侧的上部。
The
集水槽14通过第一水泵1及第一循环水管2与第一喷淋水管组3连接,集水槽14还通过第二水泵15及第二循环水管13与第二喷淋水管组12连接。
The
使用上述实施例时,在水泵作用下,第一喷淋水管组3和第二喷淋水管组12分别沿管板束侧面向下管板组6和上管板组8喷淋冷却水。同时在轴流风机10的作用下,风从进风口4首先进入低温蒸发区,带走下管板组6蒸发的水汽,风及水汽经下导向隔板7的风水折流口折流进入高温蒸发区,带走上管板组8蒸发的水汽,然后经上导向隔板9的的风水折流口进入汽水分离区,在汽水分离区,水下降回落,蒸汽从壳体上端被抽出系统,实现流经管板组的介质冷凝。
When the above embodiment is used, under the action of the water pump, the first spray
如果在壳体5内挡水板17和集水槽14之间安装三块导向隔板,相应地,应当设置上、下管板束互相串联的上、中、下三组管板组,每一管板组的一侧设置一套与集水槽14相连接的喷淋水管组。最下方管板组对应进风口4,保证喷水方向与风流向一致,水、汽经过风水折流口时折流运行。保证水、汽经过风水折流口时折流运行的结构是:相邻两块导向隔板的风水折流口位于相对的两侧,最下方导向隔板的风水折流口位于进风口4相对的一侧。
If three guide partitions are installed between the
集水槽14也可以布置在壳体5之外。
The
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103527267A (en) * | 2013-10-14 | 2014-01-22 | 西安热工研究院有限公司 | Direct air-cooling unit system with plate-type evaporative condenser unit adopted |
CN103791741A (en) * | 2014-01-20 | 2014-05-14 | 同济大学 | Phase transition plate heat exchanger |
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CN203413983U (en) * | 2013-07-19 | 2014-01-29 | 烟台珈群高效节能设备有限公司 | Plate type evaporation condenser |
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Patent Citations (6)
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US4804503A (en) * | 1987-02-18 | 1989-02-14 | Shinwa Sangyo Co., Ltd. | Counter-flow square type cooling tower |
CN201355199Y (en) * | 2009-02-26 | 2009-12-02 | 江西安晟化工科技有限公司 | Evaporative condenser |
CN103090696A (en) * | 2011-11-07 | 2013-05-08 | 黄生 | Evaporative type condenser |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103527267A (en) * | 2013-10-14 | 2014-01-22 | 西安热工研究院有限公司 | Direct air-cooling unit system with plate-type evaporative condenser unit adopted |
CN103527267B (en) * | 2013-10-14 | 2015-05-27 | 西安热工研究院有限公司 | Direct air-cooling unit system with plate-type evaporative condenser unit adopted |
CN103791741A (en) * | 2014-01-20 | 2014-05-14 | 同济大学 | Phase transition plate heat exchanger |
CN103791741B (en) * | 2014-01-20 | 2016-08-17 | 同济大学 | A kind of phase transformation plate type heat exchanger |
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