CN202719904U - A High Pressure Resistant Circular Corrugated Plate Shell Heat Exchanger - Google Patents
A High Pressure Resistant Circular Corrugated Plate Shell Heat Exchanger Download PDFInfo
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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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- 238000012546 transfer Methods 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 4
- 238000003754 machining Methods 0.000 abstract 1
- 239000012530 fluid Substances 0.000 description 11
- 238000003466 welding Methods 0.000 description 7
- 238000013461 design Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000010687 lubricating oil Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910001069 Ti alloy Inorganic materials 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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Abstract
Description
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-
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
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
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
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
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
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
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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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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2012
- 2012-06-04 CN CN2012202588175U patent/CN202719904U/en not_active Expired - Fee Related
Cited By (5)
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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