CN204438867U - The two distributor plate-type heat exchanger in a kind of diagonal angle - Google Patents
The two distributor plate-type heat exchanger in a kind of diagonal angle Download PDFInfo
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- CN204438867U CN204438867U CN201420851413.6U CN201420851413U CN204438867U CN 204438867 U CN204438867 U CN 204438867U CN 201420851413 U CN201420851413 U CN 201420851413U CN 204438867 U CN204438867 U CN 204438867U
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- 239000012530 fluid Substances 0.000 claims abstract description 25
- 239000006185 dispersion Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 description 5
- 239000003507 refrigerant Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本实用新型提供了一种对角双分配器型板式换热器,其上设有波纹片组,波纹片组包括水平180度反向层叠设置的多个波纹板,所述波纹板上设有四个角孔,其中一个角孔旁设有第一分配器,其对角角孔的侧壁上设有第二分配器;第一分配器包括环形内凸棱和外凸棱,外凸棱的高度高于内凸棱的高度,内凸棱和外凸棱之间形成流体腔;第二分配器包括与第二波纹板角孔相连通的两个轴向分配孔,分配孔之间还设有弧形分配板。本实用新型所提供的一种对角双分配器型板式换热器,通过对角设置在波纹板上的双分配器,使得流体混合充分,流体流动均匀,流动阻力低,进一步提高了板式换热器的热交换效率。
The utility model provides a diagonal double-distributor type plate heat exchanger, on which a group of corrugated sheets is provided. Four corner holes, one of which is provided with a first distributor next to the corner hole, and a second distributor is arranged on the side wall of the diagonal hole; the first distributor includes annular inner convex ribs and outer convex ribs, and the outer convex ribs The height of the inner rib is higher than that of the inner rib, and a fluid chamber is formed between the inner rib and the outer rib; the second distributor includes two axial distribution holes communicated with the corner holes of the second corrugated plate, and there is a gap between the distribution holes Equipped with curved distribution plate. The utility model provides a diagonal double distributor type plate heat exchanger, through the double distributors arranged diagonally on the corrugated plate, the fluid is fully mixed, the fluid flow is uniform, and the flow resistance is low, which further improves the efficiency of the plate heat exchanger. The heat exchange efficiency of the heater.
Description
技术领域 technical field
本实用新型涉及板式换热器制造领域,具体为一种对角双分配器型板式换热器。 The utility model relates to the field of plate heat exchanger manufacture, in particular to a diagonal double distributor type plate heat exchanger.
背景技术 Background technique
板式换热器在单相换热的工况下能够发挥其优势,但在两相换热工况中,由于气液两相流体的物性、流态等差别较大,难以实现流体均匀分配及在板间流道内流量均匀流动,当高压的液态制冷剂尤其是气液两相混合制冷剂由分配器孔喷出时,无法实现充分雾化,从而影响液态制冷剂的快速挥发,进而增加流阻,降低换热器的换热性能。另外在波纹均匀分布的板片组成的流道内,流体的流量分配不均匀,从进口到出口的直线附近区域的流速较大,越远离该区域其流速越小,流道内流量分配不均匀会导致流阻增加及换热器换热性能降低。气液两相混合制冷剂进入分配器以后,无法得到充分混合,从而使得流阻较大,流量不能有效均匀分配及在板间流道内均匀流动,从而使得换热器压降较大、换热性能降低。因此,需要进一步改进板式换热器板片和分配器的结构,提高板片的流体流动均匀性、降低流动阻力,使得冷热介质混合充分,以获得最佳的换热性能。 Plate heat exchangers can give full play to their advantages in single-phase heat exchange conditions, but in two-phase heat exchange conditions, due to the large differences in physical properties and flow states of gas-liquid two-phase fluids, it is difficult to achieve uniform fluid distribution and The flow in the channel between the plates flows evenly. When the high-pressure liquid refrigerant, especially the gas-liquid two-phase mixed refrigerant, is sprayed out from the distributor hole, it cannot achieve sufficient atomization, which affects the rapid volatilization of the liquid refrigerant and increases the flow rate. resistance, reducing the heat transfer performance of the heat exchanger. In addition, in the flow channel composed of uniformly distributed corrugated plates, the flow distribution of the fluid is uneven. The flow velocity in the area near the straight line from the inlet to the outlet is relatively high, and the farther away from this area, the smaller the flow velocity. The uneven flow distribution in the flow channel will lead to The flow resistance increases and the heat transfer performance of the heat exchanger decreases. After the gas-liquid two-phase mixed refrigerant enters the distributor, it cannot be fully mixed, resulting in a large flow resistance, and the flow cannot be effectively and evenly distributed and evenly flowed in the flow channel between the plates, resulting in a large pressure drop of the heat exchanger and poor heat transfer performance. Reduced performance. Therefore, it is necessary to further improve the structure of the plates and distributors of plate heat exchangers, improve the fluid flow uniformity of the plates, reduce the flow resistance, and fully mix the cold and hot media to obtain the best heat exchange performance.
实用新型内容 Contents of utility model
针对上述问题,本实用新型提供了一种设有新型板式换热器。 In view of the above problems, the utility model provides a novel plate heat exchanger.
本实用新型采用的技术方案是,构建一种对角双分配器型板式换热器,其上设有波纹片组,上述波纹片组包括水平180度反向层叠设置的多个波纹板,上述波纹板上设有四个角孔,其中一个角孔旁设有第一分配器,其对角角孔的侧壁上设有第二分配器;上述第一分配器包括环形内凸棱和外凸棱,上述外凸棱的高度高于内凸棱的高度,上述内凸棱和外凸棱之间形成流体腔;上述第二分配器包括与第二波纹板角孔相连通的两个轴向分配孔,上述分配孔之间还设有弧形分配板。将第一分配器和第二分配器设置于同一块板片上,减少了板式换热器使用中的零部件数量,一次通过模具将两种分配器结构冲压成型,减少了装配过程中的板片安装错误发生率。同时在板式换热器的每两层板片间设有两个流体分配器,使得流体的分配更加均匀,混合更加充分。 The technical solution adopted by the utility model is to construct a diagonal double distributor type plate heat exchanger, on which a group of corrugated sheets is provided. There are four corner holes on the corrugated plate, a first distributor is arranged beside one corner hole, and a second distributor is arranged on the side wall of the corner hole; the above-mentioned first distributor includes an annular inner rib and an outer a convex rib, the height of the outer rib is higher than that of the inner rib, and a fluid chamber is formed between the inner rib and the outer rib; the second distributor includes two shafts communicated with the corner holes of the second corrugated plate To the distribution holes, an arc-shaped distribution plate is also arranged between the above distribution holes. The first distributor and the second distributor are arranged on the same plate, which reduces the number of parts in the use of the plate heat exchanger, and the two distributor structures are stamped and formed through the mold at one time, reducing the number of plates in the assembly process The incidence of installation errors. At the same time, there are two fluid distributors between every two layers of plates in the plate heat exchanger, so that the fluid distribution is more uniform and the mixing is more sufficient.
进一步地,上述外凸棱上还设有多条介质分散槽,上述分配分散槽的槽底低于上述内凸棱的最高点,高于上述流体腔的最低点。有利于降低流动阻力的同时,强迫流体沿着远离流体分配器另一侧的板片波纹开始流动,使板间流体流量分配更加均匀,提高板片热交换效率。 Furthermore, a plurality of medium dispersion grooves are arranged on the outer rib, and the bottom of the distribution and dispersion groove is lower than the highest point of the inner rib and higher than the lowest point of the fluid chamber. It is beneficial to reduce the flow resistance and at the same time, force the fluid to start flowing along the plate corrugations on the other side away from the fluid distributor, so that the fluid flow distribution between the plates is more uniform and the heat exchange efficiency of the plates is improved.
进一步地,上述分散槽的截面为圆弧形或者椭圆弧形。 Further, the cross-section of the dispersion groove is arc-shaped or elliptical-arc.
进一步地,上述多个分散槽围绕角孔中心呈螺旋离心型分布或放射线型分布。强迫流体沿着远离流体分配器另一侧的板片波纹开始流动,使板间流体流量分配更加均匀,提高板片热交换效率。 Further, the above-mentioned multiple dispersion grooves are distributed in a spiral centrifugal type or radially around the center of the corner hole. The fluid is forced to flow along the plate corrugations on the other side away from the fluid distributor, so that the fluid flow distribution between the plates is more uniform and the heat exchange efficiency of the plates is improved.
进一步地,上述第二分配器的侧旁设有环形沉台面,上述环形沉台面与上述第二波纹板的上端面构成圆柱形空腔。主要用于充分混合。 Further, the side of the second distributor is provided with an annular countertop, and the annular countertop and the upper end surface of the second corrugated plate form a cylindrical cavity. Primarily used for thorough mixing.
进一步地,上述波纹板和第二波纹板上均设有多个位置形状匹配的凸台和凹坑。用于在装配时候卡位并卡接,使得整个波纹片组更加牢固稳定。 Further, both the above-mentioned corrugated plate and the second corrugated plate are provided with a plurality of bosses and recesses whose positions and shapes match. It is used for clamping and clamping during assembly, making the entire corrugated sheet group more firm and stable.
进一步地,上述内凸棱上还设有多条导向槽。用于流体导向和降低流动阻力。 Furthermore, a plurality of guide grooves are also provided on the above-mentioned inner rib. For fluid guidance and reducing flow resistance.
进一步地,所述沉台面上还围绕第二分配器均设有多个通孔,所述通孔的直径为1-2mm。设置多个通孔,实现流体节流降压的作用。 Further, a plurality of through holes are arranged around the second distributor on the countertop, and the diameter of the through holes is 1-2mm. A plurality of through holes are provided to realize the function of fluid throttling and pressure reduction.
与现有技术相比,本实用新型所提供的一种对角双分配器型板式换热器,通过对角设置在波纹板上的双分配器,使得流体混合充分,流体流动均匀,流动阻力低,进一步提高了板式换热器的热交换效率。 Compared with the prior art, the utility model provides a diagonal double distributor type plate heat exchanger, through the double distributors arranged diagonally on the corrugated plate, the fluid is fully mixed, the fluid flow is uniform, and the flow resistance Low, which further improves the heat exchange efficiency of the plate heat exchanger.
附图说明 Description of drawings
图1为本实用新型的立体示意图。 Fig. 1 is a perspective view of the utility model.
图2为本实用新型波纹板的结构示意图。 Fig. 2 is a structural schematic diagram of the corrugated board of the present invention.
图3为实用新型第一分配器的结构示意图。 Fig. 3 is a schematic structural view of the first dispenser of the utility model.
图4为本实用新型第二分配器的结构示意图。 Fig. 4 is a schematic structural view of the second distributor of the present invention.
具体实施方式 Detailed ways
在下面的描述中阐述了很多具体细节以便于充分理解本实用新型。但是本实用新型能够以很多不同于在此描述的其它方式来实施,本领域技术人员可以在不违背本实用新型内涵的情况下做类似推广,因此本实用新型不受下面公开的具体实施例的限制。 In the following description, numerous specific details are set forth in order to provide a full understanding of the present invention. However, the utility model can be implemented in many other ways different from those described here, and those skilled in the art can do similar promotions without violating the connotation of the utility model, so the utility model is not limited by the specific embodiments disclosed below limit.
下面结合附图和实施例,对本实用新型的具体实施方式做进一步的说明。 Below in conjunction with accompanying drawing and embodiment, the specific implementation mode of the utility model is described further.
实施例1 Example 1
在本实施例中,结合附图,对本实用新型的结构进行详细描述。 In this embodiment, the structure of the utility model is described in detail with reference to the accompanying drawings.
请参见附图,本实用新型提供的一种对角双分配器型板式换热器,所述波纹片组包括水平180度反向层叠设置的多个波纹板1,所述波纹板1上设有四个角孔,其中一个角孔旁设有第一分配器11,其对角角孔的侧壁上设有第二分配器21;第一分配器11包括环形内凸棱111和外凸棱112,外凸棱112的高度高于内凸棱111的高度,内凸棱111和外凸棱112之间形成流体腔113;第二分配器21包括与第二波纹板角孔相连通的两个轴向分配孔211,分配孔211之间还设有弧形分配板212。 Please refer to the accompanying drawings, a diagonal double distributor type plate heat exchanger provided by the utility model, the corrugated sheet group includes a plurality of corrugated plates 1 arranged horizontally and reversely stacked at 180 degrees, and the corrugated plates 1 are provided with There are four corner holes, wherein a first distributor 11 is arranged beside one corner hole, and a second distributor 21 is arranged on the side wall of its diagonal corner hole; the first distributor 11 includes an annular inner rib 111 and an outer convex Rib 112, the height of the outer rib 112 is higher than the height of the inner rib 111, a fluid cavity 113 is formed between the inner rib 111 and the outer rib 112; There are two axial distribution holes 211, and an arc-shaped distribution plate 212 is arranged between the distribution holes 211.
作为优选,外凸棱112上还设有多条介质分散槽1121,分配分散槽1121的槽底低于内凸棱111的最高点,高于流体腔113的最低点,分散槽1121的截面为圆弧形或者椭圆弧形,多个分散槽1121围绕角孔中心呈螺旋离心型分布或放射线型分布,内凸棱111上还设有多条导向槽1111。 As preferably, a plurality of medium dispersion grooves 1121 are also provided on the outer rib 112, and the groove bottom of the distribution dispersion groove 1121 is lower than the highest point of the inner rib 111, higher than the lowest point of the fluid chamber 113, and the cross section of the dispersion groove 1121 is Arc-shaped or elliptical arc-shaped, a plurality of dispersing grooves 1121 are distributed spirally centrifugally or radially around the center of the corner hole, and a plurality of guide grooves 1111 are also provided on the inner rib 111 .
作为优选,第二分配器21的侧旁设有环形沉台面213,环形沉台面213与第二波纹板1的上端面构成圆柱形空腔。所述沉台面213上还围绕第二分配器21均设有多个通孔2131,所述通孔2131的直径为1-2mm。 Preferably, the side of the second distributor 21 is provided with an annular countertop 213 , and the annular countertop 213 and the upper end surface of the second corrugated plate 1 form a cylindrical cavity. The countertop 213 is also provided with a plurality of through holes 2131 around the second distributor 21, and the diameter of the through holes 2131 is 1-2 mm.
作为优选,波纹板1和第二波纹板2上均设有多个位置形状匹配的凸台和凹坑。方便装配卡接,使得板式换热器层间更加牢固稳定。 Preferably, both the corrugated plate 1 and the second corrugated plate 2 are provided with a plurality of bosses and pits whose positions and shapes match. It is convenient to assemble and clamp, making the interlayer of the plate heat exchanger more firm and stable.
本实用新型虽然以较佳实施例公开如上,但其并不是用来限定本实用新型,任何本领域技术人员在不脱离本实用新型的精神和范围内,都可以做出可能的变动和修改,因此本实用新型的保护范围应当以本实用新型权利要求所界定的范围为准。 Although the utility model is disclosed as above with preferred embodiments, it is not used to limit the utility model, and any person skilled in the art can make possible changes and modifications without departing from the spirit and scope of the utility model. Therefore, the protection scope of the utility model should be defined by the claims of the utility model.
Claims (8)
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106556263A (en) * | 2015-09-28 | 2017-04-05 | 丹佛斯微通道换热器(嘉兴)有限公司 | Plate type heat exchanger |
CN106643236A (en) * | 2015-10-29 | 2017-05-10 | 达纳加拿大公司 | Structural support element in heat exchangers |
CN107388876A (en) * | 2017-08-21 | 2017-11-24 | 江苏远卓设备制造有限公司 | A kind of plate type heat exchange piece |
CN110186300A (en) * | 2019-06-27 | 2019-08-30 | 浙江银轮机械股份有限公司 | Plate, plate component and heat exchanger |
CN112313466A (en) * | 2018-06-28 | 2021-02-02 | 阿法拉伐股份有限公司 | Heat transfer plate and gasket |
WO2021147479A1 (en) * | 2020-01-22 | 2021-07-29 | 丹佛斯有限公司 | Plate heat exchanger |
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2014
- 2014-12-30 CN CN201420851413.6U patent/CN204438867U/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106556263A (en) * | 2015-09-28 | 2017-04-05 | 丹佛斯微通道换热器(嘉兴)有限公司 | Plate type heat exchanger |
CN106556263B (en) * | 2015-09-28 | 2019-01-25 | 丹佛斯微通道换热器(嘉兴)有限公司 | Plate heat exchanger |
CN106643236A (en) * | 2015-10-29 | 2017-05-10 | 达纳加拿大公司 | Structural support element in heat exchangers |
CN107388876A (en) * | 2017-08-21 | 2017-11-24 | 江苏远卓设备制造有限公司 | A kind of plate type heat exchange piece |
CN107388876B (en) * | 2017-08-21 | 2023-12-05 | 江苏远卓设备制造有限公司 | Plate type heat exchange plate |
CN112313466A (en) * | 2018-06-28 | 2021-02-02 | 阿法拉伐股份有限公司 | Heat transfer plate and gasket |
CN110186300A (en) * | 2019-06-27 | 2019-08-30 | 浙江银轮机械股份有限公司 | Plate, plate component and heat exchanger |
WO2021147479A1 (en) * | 2020-01-22 | 2021-07-29 | 丹佛斯有限公司 | Plate heat exchanger |
SE2050164A1 (en) * | 2020-02-14 | 2021-08-15 | Alfa Laval Corp Ab | A heat exchanger plate, and a plate heat exchanger |
WO2021160370A1 (en) * | 2020-02-14 | 2021-08-19 | Alfa Laval Corporate Ab | A heat exchanger plate, and a plate heat exchanger |
SE545536C2 (en) * | 2020-02-14 | 2023-10-17 | Alfa Laval Corp Ab | A heat exchanger plate, and a plate heat exchanger |
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