CN202719904U - A High Pressure Resistant Circular Corrugated Plate Shell Heat Exchanger - Google Patents

A High Pressure Resistant Circular Corrugated Plate Shell Heat Exchanger Download PDF

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CN202719904U
CN202719904U CN2012202588175U CN201220258817U CN202719904U CN 202719904 U CN202719904 U CN 202719904U CN 2012202588175 U CN2012202588175 U CN 2012202588175U CN 201220258817 U CN201220258817 U CN 201220258817U CN 202719904 U CN202719904 U CN 202719904U
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shell
plate
corrugated
corrugated plate
heat exchanger
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丁铭
王佳卓
阎昌琪
石帅
陈哲雨
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Harbin Engineering University
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Harbin Engineering University
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Abstract

The utility model aims to provide a high-pressure-resistant circular corrugated plate shell-and-plate heat exchanger, which comprises a shell, cover plates, a corrugated plate bundle, flow guide blocks and supporting plates, wherein the corrugated plate bundle comprises corrugated plates and is fixedly arranged in the shell through the supporting plates; the two ends of the shell are sealed by the cover plates; the shell is provided with a shell pass outlet and a shell pass inlet; the cover plates are provided with plate pass inlets and plate pass outlets; an annular region between the shell and the corrugated plate bundle is divided into a shell pass inlet chamber and a shell pass outlet chamber by the flow guide blocks; the shell pass inlet is communicated with the shell pass inlet chamber; the shell pass outlet is communicated with the shell pass outlet chamber; the corrugated plate bundle is provided with angular holes; and the plate pass inlet and the plate pass outlet are communicated through the angular holes of the corrugated plate bundle. The high-pressure-resistant circular corrugated plate shell-and-plate heat exchanger has the advantages of high bearing capacity, high heat exchange efficiency, compact structure, large heat transfer area in a unit volume, wide material selection range, wide application range, simple machining and easiness in mounting.

Description

一种耐高压的圆形波纹板板壳式换热器A High Pressure Resistant Circular Corrugated Plate Shell Heat Exchanger

技术领域 technical field

本实用新型涉及的是一种强化换热技术领域的换热器。The utility model relates to a heat exchanger in the technical field of enhanced heat exchange.

背景技术 Background technique

板式换热器由于具有换热效率高、结构紧凑的特点而广泛应用于能源、动力、供热、制冷等多种领域。随着板式换热器技术的成熟,在一些领域已经取代了传统的管壳式换热器。但现有的矩形板式换热器普遍存在承压能力较低的问题。在石油化工等常见压力较高的领域中,板式换热器的应用受到了极大的限制。开发一种能够承受高压且结构紧凑的板式换热器在能源动力领域有着广泛的应用前景。目前虽然存在一些全焊接的板壳式换热器,但其工作压力一般不超过4.5MPa,且体积相对较大,紧凑度不高。这些全焊接的板壳式换热器以矩形板片作为传热元件,并将板束置于矩形或圆形的壳体中以提升承压性能。这种板式换热器承压能力有限且体积较大。Plate heat exchangers are widely used in energy, power, heating, refrigeration and other fields due to their high heat transfer efficiency and compact structure. With the maturity of plate heat exchanger technology, it has replaced the traditional shell and tube heat exchanger in some fields. However, the existing rectangular plate heat exchanger generally has the problem of low pressure bearing capacity. In petrochemical and other common high-pressure fields, the application of plate heat exchangers has been greatly restricted. Developing a plate heat exchanger that can withstand high pressure and has a compact structure has broad application prospects in the field of energy and power. Although there are some fully welded plate and shell heat exchangers at present, their working pressure generally does not exceed 4.5MPa, and their volume is relatively large and their compactness is not high. These fully welded plate and shell heat exchangers use rectangular plates as heat transfer elements, and the plate bundles are placed in rectangular or circular shells to improve pressure performance. This kind of plate heat exchanger has limited pressure bearing capacity and large volume.

普通板式换热器中两种介质的通道结构相同,对于两侧换热介质物性相差较大的一些工况,会出现设计上的不匹配,进而造成体积和材料上的浪费。例如当利用水冷却高粘度润滑油时,由于润滑油的粘度远高于水的粘度,相同流量下润滑油的流动阻力会远高于冷却水的流动阻力,通常润滑油的流动阻力达到设计要求的上限时,冷却水侧的流动阻力还远未达限值,这就造成了设计上的浪费。In ordinary plate heat exchangers, the channel structure of the two media is the same. For some working conditions where the physical properties of the heat exchange media on both sides are quite different, there will be design mismatches, which will result in waste of volume and materials. For example, when using water to cool high-viscosity lubricating oil, since the viscosity of the lubricating oil is much higher than that of water, the flow resistance of the lubricating oil will be much higher than that of the cooling water at the same flow rate, and usually the flow resistance of the lubricating oil meets the design requirements When the upper limit is reached, the flow resistance on the cooling water side is far from the limit value, which causes design waste.

发明内容 Contents of the invention

本实用新型的目的在于提供适用于不同种类流体间换热、尤其适合于热物性相差较大的两种介质间换热的一种耐高压的圆形波纹板板壳式换热器。The purpose of the utility model is to provide a high-pressure-resistant circular corrugated plate-shell heat exchanger suitable for heat exchange between different types of fluids, especially for heat exchange between two media with large thermal and physical properties differences.

本实用新型的目的是这样实现的:The purpose of this utility model is achieved in that:

本实用新型一种耐高压的圆形波纹板板壳式换热器,其特征是:包括壳体、盖板、波纹板板束、导流块、支撑板,波纹板板束包括波纹板,波纹板板束通过支撑板固定在壳体里,壳体两端通过盖板密封,壳体上设置壳程出口、壳程进口,盖板上设置板程进口、板程出口,外壳与波纹板板束间的环形区域被导流块分隔成壳程进口腔室和壳程出口腔室,壳程进口连通壳程进口腔室,壳程出口连通壳程出口腔室,波纹板板束上开有角孔,板程进口和板程出口通过波纹板板束的角孔相连通。The utility model is a high-pressure-resistant circular corrugated plate-shell heat exchanger, which is characterized in that it includes a shell, a cover plate, a corrugated plate bundle, a diversion block, a support plate, and the corrugated plate bundle includes a corrugated plate, The corrugated plate bundle is fixed in the shell through the supporting plate, the two ends of the shell are sealed by the cover plate, the shell side outlet and the shell side inlet are set on the shell, the plate side inlet and the plate side outlet are set on the cover plate, the shell and the corrugated plate The annular area between the plate bundles is divided into a shell-side inlet chamber and a shell-side outlet chamber by a deflector block. The shell-side inlet is connected to the shell-side inlet chamber, and the shell-side outlet is connected to the shell-side outlet chamber. There are corner holes, and the board side inlet and board side outlet are connected through the corner holes of the corrugated board bundle.

本实用新型还可以包括:The utility model can also include:

1、两个波纹板压在一起形成板片对,板片对内部形成壳程出口、壳程进口之间的板间通道,板片对连接在一起形成波纹板板束,板片对之间形成板程进口、板程出口之间的板间通道。1. Two corrugated plates are pressed together to form a plate pair. The plate pair forms an inter-plate channel between the shell side outlet and the shell side inlet. The plate pairs are connected together to form a corrugated plate bundle. Between the plate pairs Form the inter-board channel between the board-side inlet and the board-side outlet.

2、所述的板程进口位于换热器本体的上端,板程出口位于换热器本体的下端,壳程出口位于外壳上板程进口一侧,壳程进口位于外壳上板程出口一侧。2. The plate side inlet is located at the upper end of the heat exchanger body, the plate side outlet is located at the lower end of the heat exchanger body, the shell side outlet is located on the side of the plate side inlet on the shell, and the shell side inlet is located on the side of the plate side outlet on the shell .

3、波纹板采用平直波纹或人字形波纹的圆形板片,波纹板两面波纹高度不同。3. The corrugated plate adopts a circular plate with straight corrugation or herringbone corrugation, and the corrugation heights on both sides of the corrugated plate are different.

本实用新型的优势在于:The utility model has the advantages of:

1、承压能力强。板片采用全焊接的方式相连接,不用密封垫片,承压能力比可拆式和钎焊式板式换热器强。普通的矩形板片承压时会出现应力集中。采用的圆形板片承压时应力分布均匀,不易因出现局部应力集中而造成破损泄露,比普通的矩形板片承压能力更好。此外,采用板壳式设计,将板束包围在壳体内,进一步提升了密封性能和承压能力。1. Strong pressure bearing capacity. The plates are connected by full welding without sealing gaskets, and the pressure bearing capacity is stronger than that of detachable and brazed plate heat exchangers. Stress concentration occurs when ordinary rectangular plates are under pressure. When the circular plate is under pressure, the stress distribution is uniform, and it is not easy to cause damage and leakage due to local stress concentration, and its pressure bearing capacity is better than that of ordinary rectangular plates. In addition, the plate and shell design is adopted to enclose the plate bundle in the shell, which further improves the sealing performance and pressure bearing capacity.

2、换热效率高。板束内的板间通道为人字形或双人字形波纹通道,交叉接触点多。流体在板间通道内绕接触点成涡流流动,扰流强烈,能有效破坏粘性介质流动时的边界层,起到强化传热的作用。2. High heat exchange efficiency. The channel between plates in the plate bundle is a herringbone or double herringbone corrugated channel with many cross contact points. The fluid flows in a vortex around the contact point in the channel between the plates, and the turbulence is strong, which can effectively destroy the boundary layer when the viscous medium flows, and play a role in enhancing heat transfer.

3、结构紧凑,单位体积内的传热面积大。本实用新型中的波纹板排列紧密,且换热器整体结构简单紧凑,在相同体积下,本实用新型比管壳式换热器具有更大的传热面积。与采用矩形板片的板壳式换热器相比,结构更为紧凑。3. Compact structure, large heat transfer area per unit volume. The corrugated plates in the utility model are closely arranged, and the overall structure of the heat exchanger is simple and compact. Under the same volume, the utility model has a larger heat transfer area than the shell-and-tube heat exchanger. Compared with the plate and shell heat exchanger with rectangular plates, the structure is more compact.

4、选材范围广。本实用新型中的波纹板可以采用多种不同材料,例如各种型号的不锈钢、铜合金、钛合金等,以适用于不同种类的换热介质。4. Wide selection of materials. The corrugated plate in the utility model can adopt many different materials, such as various types of stainless steel, copper alloy, titanium alloy, etc., so as to be suitable for different types of heat exchange media.

5、适用范围广。圆形波纹板两侧波纹高度不同,在两侧介质流量、物性参数相差较大时具有较强的适用性。且换热器可以根据实际需要将两侧介质设计成多种流程组合。5. Wide application range. The corrugation heights on both sides of the circular corrugated plate are different, and it has strong applicability when the medium flow and physical parameters on both sides are quite different. And the heat exchanger can be designed with various process combinations for the media on both sides according to actual needs.

6、加工简单、易于安装。本实用新型所述的非对称通道圆形波纹板加工方便快捷,生产周期短,成本低,特别适合于工业化批量生产。6. Simple processing and easy installation. The asymmetric channel circular corrugated plate described in the utility model is convenient and quick to process, has a short production cycle and low cost, and is especially suitable for industrial batch production.

综上所述,本实用新型是一种兼备管壳式换热器耐压能力高和板式换热器紧凑度强、传热系数大特点的新型板壳式换热器,而且具有使用范围广、可靠性高、易于制造的特点,具有良好的发展应用前景。In summary, the utility model is a new type of plate-shell heat exchanger with the characteristics of high pressure resistance of shell-and-tube heat exchangers, high compactness and large heat transfer coefficient of plate heat exchangers, and has a wide range of applications. , high reliability, easy to manufacture, and has good development and application prospects.

附图说明 Description of drawings

图1为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;

图2为A-A剖视图;Fig. 2 is A-A sectional view;

图3为两侧介质在本实用新型内流动分配的示意图;Fig. 3 is a schematic diagram of flow distribution of media on both sides in the utility model;

图4为板片对焊接的结构示意图;Fig. 4 is a structural schematic diagram of plate butt welding;

图5为板束焊接的结构示意图。Figure 5 is a structural schematic diagram of plate beam welding.

具体实施方式 Detailed ways

下面结合附图举例对本实用新型做更详细地描述:The utility model is described in more detail below in conjunction with accompanying drawing example:

结合图1~5,本实用新型由板程进口1、板程出口7、壳程进口9、壳程出口3、壳程进口腔室14、壳程出口腔室12、波纹板板束5、支撑板6、10、导流块11和13、两侧盖板2和8以及壳体4等部件组成。波纹板板束5与支撑板6、10通过角孔相焊接,并通过支撑板6、10置于壳体4内。板束5两端被盖板2、8压紧固定。盖板2、8与壳体4焊接形成完整的外壳,将波纹板板束5及支撑板6、10包围在其内部。外壳与板束间的环形区域被导流块11、13分隔成壳程进口腔室14和壳程出口腔室12。壳体4上带有壳程进口9和壳程出口3。壳程进口和壳程出口分别与壳程进口腔室和壳程出口腔室连通。两侧盖板2、8上分别带有板程进口1和板程出口7。板程进口和板程出口分别与板束的两条角孔通道相连通。In conjunction with Figures 1 to 5, the utility model consists of a board-side inlet 1, a board-side outlet 7, a shell-side inlet 9, a shell-side outlet 3, a shell-side inlet chamber 14, a shell-side outlet chamber 12, corrugated board bundles 5, It is composed of supporting plates 6, 10, deflector blocks 11 and 13, cover plates 2 and 8 on both sides, and housing 4 and other components. The corrugated plate bundle 5 is welded to the support plates 6, 10 through corner holes, and placed in the housing 4 through the support plates 6, 10. The two ends of the plate bundle 5 are compressed and fixed by the cover plates 2 and 8 . The cover plates 2, 8 are welded with the shell 4 to form a complete shell, which encloses the corrugated plate bundle 5 and the supporting plates 6, 10 inside. The annular area between the shell and the plate bundle is divided into a shell-side inlet chamber 14 and a shell-side outlet chamber 12 by guide blocks 11 and 13 . The shell 4 has a shell side inlet 9 and a shell side outlet 3 . The shell-side inlet and the shell-side outlet communicate with the shell-side inlet chamber and the shell-side outlet chamber respectively. The board pass inlet 1 and the board pass outlet 7 are respectively provided on the cover plates 2 and 8 on both sides. The plate way inlet and the plate way outlet are respectively connected with the two corner hole channels of the plate bundle.

波纹板板束5由圆形波纹板15组焊而成。图4、图5是圆形波纹板组焊过程的剖视图。结合图2、图4、图5,圆形波纹板15、17的两侧波纹高度不同,两波纹板紧压在一起并沿角孔外周的翼边焊接16、19,形成板片对20。圆形波纹板15、17焊接成板片对后,其内部形成壳程的板间通道18。圆形波纹板如上所述两两焊接成板片对后,多个板片对之间再焊接成波纹板板束。板片对20、22紧压在一起,并通过波纹板外周的翼边焊接23。两对板片对之间的通道形成板程的板间通道21。The corrugated plate bundle 5 is welded by circular corrugated plates 15 . Figure 4 and Figure 5 are cross-sectional views of the welding process of circular corrugated plates. 2 , 4 , and 5 , the corrugations on both sides of the circular corrugated plates 15 and 17 have different heights. The two corrugated plates are pressed together and welded 16 and 19 along the edges of the corner holes to form a plate pair 20 . After the circular corrugated plates 15, 17 are welded into a plate pair, an inter-plate channel 18 of the shell side is formed inside it. After the circular corrugated plates are welded two by two to form a plate pair, multiple plate pairs are welded to form a corrugated plate bundle. The sheet pairs 20, 22 are pressed together and welded 23 through the edges of the corrugated sheet periphery. The channel between the two pairs of plates forms the inter-plate channel 21 of the plate side.

流体可以从板片对内部两张波纹板的外周间的缝隙进入壳程的板间通道18。角孔中的流体则可以通过相邻两对板片对角孔间的缝隙进入板程的板间通道21。如图4所示,由于采用的波纹板两侧波纹高度不同,板束的相邻通道18、21的流道宽度不同。在两侧介质流量或热物性相差较大时具有较强的适用性。Fluid can enter the inter-plate channel 18 on the shell side from the gap between the outer peripheries of the two corrugated plates inside the plate pair. The fluid in the corner holes can enter the inter-plate channel 21 of the plate side through the gap between the diagonal holes of two adjacent pairs of plates. As shown in FIG. 4 , due to the different corrugation heights on both sides of the corrugated plate used, the flow channel widths of the adjacent channels 18 and 21 of the plate bundle are different. It has strong applicability when the flow rate or thermal properties of the media on both sides are quite different.

图3是两侧介质在本实用新型内流动分配的示意图。为方便观察流体在板间通道内的流动,图中用直线代表波纹板的剖面图。结合图3和图1、2,板程流体从板程进口1流入板束的角孔通道。结合图4,板程流体通过角孔通道分配流量,并通过各板片对之间的角孔缝隙进入板程的板间通道21,经换热后进入另一侧角孔通道。最终板程流体从流出板程出口7流出换热器。壳程流体从壳程进口9流入壳程进口腔室14。壳程流体在壳程进口腔室中进行分配,并通过各板片对内部的周向缝隙进入壳程的板间通道18,经换热后进入壳程出口腔室12。最终壳程流体从壳程出口3流出换热器。两种介质分别在相邻的板间通道内逆向流动,并通过波纹板换热。Fig. 3 is a schematic diagram of flow distribution of media on both sides in the utility model. In order to facilitate the observation of the flow of fluid in the channel between the plates, the cross-sectional view of the corrugated plate is represented by a straight line in the figure. Combining Figure 3 with Figures 1 and 2, the board side fluid flows from the board side inlet 1 into the corner hole channel of the board bundle. Referring to FIG. 4 , the plate-side fluid distributes flow through the corner hole channels, and enters the inter-plate channel 21 of the plate side through the corner hole gaps between each plate pair, and enters the corner hole channel on the other side after heat exchange. Finally, the plate-side fluid flows out of the heat exchanger from the out-flow plate-side outlet 7. The shell side fluid flows from the shell side inlet 9 into the shell side inlet chamber 14 . The shell-side fluid is distributed in the shell-side inlet chamber, and enters the shell-side inter-plate channel 18 through the circumferential gaps inside each plate pair, and enters the shell-side outlet chamber 12 after heat exchange. Finally, the shell side fluid flows out of the heat exchanger from the shell side outlet 3. The two media flow in opposite directions in the channels between the adjacent plates respectively, and exchange heat through the corrugated plates.

所述的板束5由板片对20组焊而成。每个板片对20都由两片非对称的圆形波纹板通过两个角孔焊接而成。板片对20之间再通过板片的圆形外周焊接,多组板片对20焊接在一起形成圆柱形板束。组成板片对20的两波纹板间的内部通道为壳程通道,相邻板片对20间的通道为板程通道。壳程通道与板程通道可以根据实际需要设计成不同的宽度。The plate bundle 5 is welded by plate pairs 20 . Each plate pair 20 is formed by welding two asymmetric circular corrugated plates through two corner holes. The plate pairs 20 are welded through the circular periphery of the plates, and multiple sets of plate pairs 20 are welded together to form a cylindrical plate bundle. The inner channel between the two corrugated plates forming the plate pair 20 is the shell side channel, and the channel between the adjacent plate pairs 20 is the plate side channel. The shell-side channel and plate-side channel can be designed with different widths according to actual needs.

所述的非对称圆形波纹板,中心换热区域为倾斜的平直波纹或人字形波纹,波纹板两面波纹高度不同。波纹板周边为焊接用的翼边;翼边向板片的一侧突起且与该侧面上的波纹相齐平。波纹板两端相对开有两个圆形角孔,角孔外周设有焊接用的翼边;角孔翼边向板片的另一侧突起且另一侧面上的波纹相齐平。In the asymmetric circular corrugated plate, the central heat exchange area is inclined straight corrugated or herringbone corrugated, and the two sides of the corrugated plate have different corrugated heights. The periphery of the corrugated plate is a flange for welding; the flange protrudes to one side of the plate and is flush with the corrugation on the side. There are two circular corner holes opposite to each other at both ends of the corrugated plate, and the outer periphery of the corner holes is provided with a wing for welding; the wing of the corner hole protrudes to the other side of the plate and the corrugation on the other side is flush.

所述的支撑板10为一定厚度的圆形不锈钢板。支撑板6、10布置在板束的两端,其直径与壳体内径相配合。支撑板6、10上开有一个圆形孔。圆孔的直径与波纹板的角孔直径相同,其位置也与波纹板上角孔的位置相对应。支撑板与板束通过角孔进行焊接。支撑板对板束起支撑定位作用。The support plate 10 is a circular stainless steel plate with a certain thickness. Support plates 6, 10 are arranged at both ends of the plate bundle, and their diameters match the inner diameter of the housing. Have a circular hole on the support plate 6,10. The diameter of the round hole is the same as that of the corner hole on the corrugated plate, and its position corresponds to the position of the corner hole on the corrugated plate. The support plate and the plate bundle are welded through corner holes. The support plate plays a role of supporting and positioning the plate bundle.

所述的盖板2、8为较厚的圆形钢板。其上开有圆形孔,圆孔位置与支撑板6、10上孔的位置相对应。盖板上带有板程进口与板程出口。盖板把壳体中的板束紧紧的压在一起,起到承压的作用。The cover plates 2, 8 are thicker circular steel plates. There are circular holes on it, and the positions of the circular holes correspond to the positions of the holes on the support plates 6,10. The cover plate is provided with a board pass inlet and a board pass outlet. The cover plate tightly presses the plate bundles in the shell together to play the role of pressure bearing.

Claims (5)

1.一种耐高压的圆形波纹板板壳式换热器,其特征是:包括壳体、盖板、波纹板板束、导流块、支撑板,波纹板板束包括波纹板,波纹板板束通过支撑板固定在壳体里,壳体两端通过盖板密封,壳体上设置壳程出口、壳程进口,盖板上设置板程进口、板程出口,外壳与波纹板板束间的环形区域被导流块分隔成壳程进口腔室和壳程出口腔室,壳程进口连通壳程进口腔室,壳程出口连通壳程出口腔室,波纹板板束上开有角孔,板程进口和板程出口通过波纹板板束的角孔相连通。1. A high-pressure-resistant circular corrugated plate-shell heat exchanger is characterized in that it includes a shell, a cover plate, a corrugated plate bundle, a deflector block, and a support plate, and the corrugated plate bundle includes corrugated plates, corrugated plates, and corrugated plates. The plate bundle is fixed in the shell through the support plate, the two ends of the shell are sealed by the cover plate, the shell side outlet and the shell side inlet are set on the shell, the plate side inlet and the plate side outlet are set on the cover plate, the shell and the corrugated plate plate The annular area between the beams is divided into a shell-side inlet chamber and a shell-side outlet chamber by a deflector block. The shell-side inlet is connected to the shell-side inlet chamber, and the shell-side outlet is connected to the shell-side outlet chamber. The corner hole, the board side inlet and the board side outlet are connected through the corner hole of the corrugated plate bundle. 2.根据权利要求1所述的一种耐高压的圆形波纹板板壳式换热器,其特征是:两个波纹板压在一起形成板片对,板片对内部形成壳程出口、壳程进口之间的板间通道,板片对连接在一起形成波纹板板束,板片对之间形成板程进口、板程出口之间的板间通道。2. A high-pressure-resistant circular corrugated plate-shell heat exchanger according to claim 1, characterized in that: two corrugated plates are pressed together to form a plate pair, and the inside of the plate pair forms a shell-side outlet, The interplate channel between the shell side inlet, the plate pair is connected together to form a corrugated plate bundle, and the plate pair forms the interplate channel between the plate side inlet and the plate side outlet. 3.根据权利要求1或2所述的一种耐高压的圆形波纹板板壳式换热器,其特征是:所述的板程进口位于换热器本体的上端,板程出口位于换热器本体的下端,壳程出口位于外壳上板程进口一侧,壳程进口位于外壳上板程出口一侧。3. A high-pressure resistant circular corrugated plate plate-and-shell heat exchanger according to claim 1 or 2, characterized in that: the plate side inlet is located at the upper end of the heat exchanger body, and the plate side outlet is located at the upper end of the heat exchanger body. At the lower end of the heater body, the shell side outlet is located on the side of the board side inlet on the shell, and the shell side inlet is located on the side of the board side outlet on the shell. 4.根据权利要求1或2所述的一种耐高压的圆形波纹板板壳式换热器,其特征是:波纹板采用平直波纹或人字形波纹的圆形板片,波纹板两面波纹高度不同。4. A high-pressure-resistant circular corrugated plate-shell heat exchanger according to claim 1 or 2, characterized in that: the corrugated plate adopts a circular plate with straight corrugation or herringbone corrugation, and the two sides of the corrugated plate are The corrugation varies in height. 5.根据权利要求3所述的一种耐高压的圆形波纹板板壳式换热器,其特征是:波纹板采用平直波纹或人字形波纹的圆形板片,波纹板两面波纹高度不同。5. A high-pressure-resistant circular corrugated plate plate-shell heat exchanger according to claim 3, characterized in that: the corrugated plate adopts circular plates with straight corrugations or herringbone corrugations, and the height of the corrugations on both sides of the corrugated plate is different.
CN2012202588175U 2012-06-04 2012-06-04 A High Pressure Resistant Circular Corrugated Plate Shell Heat Exchanger Expired - Fee Related CN202719904U (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102706188A (en) * 2012-06-04 2012-10-03 哈尔滨工程大学 High-pressure resistant lamella heat exchanger adopting round corrugated plates
CN103673694A (en) * 2013-12-05 2014-03-26 上海热泰能源技术有限公司 Falling-film shell-and-plate heat exchanger
CN106813102A (en) * 2015-12-02 2017-06-09 深圳中燃哈工大燃气技术研究院有限公司 LNG gas stations BOG minisize thermoelectric combined production devices
WO2018019182A1 (en) * 2016-07-28 2018-02-01 恒丰工程(香港)有限公司 Side-flow plate and shell-type heat exchanging plate and multi-flow detachable plate and shell-type heat exchanger
CN107990762A (en) * 2016-10-26 2018-05-04 普劳斯特株式会社 The plate heat exchanger of disk beam body formula

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102706188A (en) * 2012-06-04 2012-10-03 哈尔滨工程大学 High-pressure resistant lamella heat exchanger adopting round corrugated plates
CN103673694A (en) * 2013-12-05 2014-03-26 上海热泰能源技术有限公司 Falling-film shell-and-plate heat exchanger
CN106813102A (en) * 2015-12-02 2017-06-09 深圳中燃哈工大燃气技术研究院有限公司 LNG gas stations BOG minisize thermoelectric combined production devices
WO2018019182A1 (en) * 2016-07-28 2018-02-01 恒丰工程(香港)有限公司 Side-flow plate and shell-type heat exchanging plate and multi-flow detachable plate and shell-type heat exchanger
CN107990762A (en) * 2016-10-26 2018-05-04 普劳斯特株式会社 The plate heat exchanger of disk beam body formula

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