WO2008151497A1 - Échangeur thermique de type à plaques-ailettes sans bande d'étanchéité - Google Patents

Échangeur thermique de type à plaques-ailettes sans bande d'étanchéité Download PDF

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Publication number
WO2008151497A1
WO2008151497A1 PCT/CN2008/000011 CN2008000011W WO2008151497A1 WO 2008151497 A1 WO2008151497 A1 WO 2008151497A1 CN 2008000011 W CN2008000011 W CN 2008000011W WO 2008151497 A1 WO2008151497 A1 WO 2008151497A1
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WO
WIPO (PCT)
Prior art keywords
heat exchange
fins
heat exchanger
plate
fin
Prior art date
Application number
PCT/CN2008/000011
Other languages
English (en)
French (fr)
Inventor
Zhixian Miao
Xiang Ling
Faqing Niu
Original Assignee
Zhixian Miao
Xiang Ling
Faqing Niu
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhixian Miao, Xiang Ling, Faqing Niu filed Critical Zhixian Miao
Priority to DK08700571.6T priority Critical patent/DK2172728T3/en
Priority to EP08700571.6A priority patent/EP2172728B1/en
Priority to JP2010511473A priority patent/JP2010529408A/ja
Priority to US12/602,502 priority patent/US9453685B2/en
Publication of WO2008151497A1 publication Critical patent/WO2008151497A1/zh

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/025—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being corrugated, plate-like elements
    • F28F3/027—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being corrugated, plate-like elements with openings, e.g. louvered corrugated fins; Assemblies of corrugated strips
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2215/00—Fins
    • F28F2215/04—Assemblies of fins having different features, e.g. with different fin densities

Definitions

  • the invention relates to the field of heat exchangers, in particular to a sealless plate fin heat exchanger. Background technique
  • the fins are placed in the heat exchanger plate in a manner that the fins are cut to meet the heat exchange medium and form a fin arrangement.
  • the heat exchange medium can smoothly flow through the fins and exchange heat.
  • Patent No. 20061 0039927. 1 and Patent No. 02828683. 9 are in the form of fins shown in the drawings of the specification.
  • the object of the present invention is to provide a non-sealing plate fin-changing method for high heat exchange efficiency, small volume and weight, low cost, and medium for heat exchange with phase change properties for the above problems existing in the prior art. Heater.
  • a technical solution for achieving the object of the present invention is: a sealless plate-fin heat exchanger comprising an outer baffle, a nozzle, a plurality of heat exchanger plates provided with fins, and a peripheral sealing bevel, characterized in that In a plurality of heat exchanger plates provided with fins, at least one heat exchange fin on the flow-through layer of the heat exchange medium is disposed laterally.
  • the lateral arrangement of the heat exchange fins on the heat exchange plate refers to the undulation direction of the heat exchange fins and The overall flow direction of the heat exchange medium in the heat exchanger is parallel.
  • the conventional placement direction of the heat exchange fins is rotated by 90°, so that the pitch fracture section of the heat exchange fins is parallel to the total rest direction of the heat exchange medium in the heat exchanger.
  • the heat exchange shield is blocked and interfered by the raised portions of the fins in the heat exchange fins, so that the heat exchange medium passes through the slits on the fins or through the fins
  • the heat exchange medium forms a continuous S-shaped flow trend in the fins placed horizontally on each heat exchange layer, and the purpose is to increase the respective fluid resistance of the heat exchange medium.
  • the heat exchange efficiency of the heat exchange medium between the fins and the heat exchange plates thereby reducing the number of heat exchange plates and heat exchange fins, reducing the volume, weight and cost of the product, and satisfying the phase change The nature of the medium for heat transfer requirements.
  • the unsealed plate-fin heat exchanger after achieving the technical solution of the present invention can be mainly used in evaporators and condensers and other heat exchange environments, and is particularly suitable for various refrigerants having two-phase properties in the refrigeration industry. Heat exchange.
  • angular hole seals In the traditional unsealed plate-fin heat exchanger, there are many forms of angular hole seals; some of the angular hole sealing methods adopt the plate hydraulic method, so that the planes around the corner holes for the heat exchange medium are sealed on the low plane. In the high plane, the height between the low plane and the high plane is equal to the height of the heat exchange fin.
  • Some corner hole sealing methods are provided with a joint sealing block on a plane for sealing the heat exchange medium around the corner hole, and the thickness of the joint sealing block is equal to the height of the heat exchange fin.
  • Some corner hole sealing methods are provided with a corner hole sealing ring on a plane for sealing the heat exchange medium around each other at a single corner hole, and the thickness of the sealing ring is equal to the height of the heat exchange fin.
  • some heat exchanger plates have a surface compounded with a low melting point.
  • the plate of the solder, and the material of the heat exchange fin is a general foil material, and the fin material has no low melting point solder.
  • some heat exchange plates use a general plate material without solder on the surface, but a low melting point solder is compounded on the foil of the heat exchange fin.
  • some heat exchange plates use a general plate with no solder on the surface, and the material surface of the heat exchange fins is also a general foil material without a low melting point solder, but in the heat exchange A foil-like low-melting, solder is applied between the plate and the heat exchange fin.
  • the heat exchange fins include various types of sawtooth type heat exchange fins and straight punch type heat exchange fins.
  • the fluid layers respectively correspond to the same type of heat exchange fins or different specifications.
  • Heat exchange fins that is, in the same heat exchanger, the different heat exchange mediums are different.
  • the fluid level can be the same size of heat exchange fins, or different heat exchanger fins can be used.
  • the specifications of the heat exchange fins generally refer to the height of the fins, the material thickness and the pitch, etc.
  • the specifications include the length of the slit and the like.
  • the specifications include parameters such as the hole diameter and the hole pitch.
  • each fluid level corresponds to the same type of heat exchange fins or different types.
  • Heat exchange fins in the same heat exchanger, different fluid layers corresponding to different heat exchange mediums may adopt the same type of heat exchange fins, and may also be heat exchange fins of the same specification or different specifications, or may be different. Type of heat exchange fins.
  • At least one heat exchange shield is provided in the same heat exchanger
  • a combination of heat exchange fins of different specifications or different types are placed horizontally. That is, in the same heat exchanger, in the different fluid layers corresponding to different heat exchange mediums, at least on each heat exchange plate of a certain heat exchange medium, the sawtooth type with different specifications can be placed horizontally at the same time.
  • Heat exchange fins and fins of the type of heat transfer fins are provided on each heat exchange plate of the circulation level.
  • the heat exchange fin combinations having different specifications or different types are placed horizontally and in-line. That is, in the same heat exchanger, in the different fluid layers corresponding to different heat exchange mediums, at least on each heat exchange plate of a certain heat exchange medium, the sawtooth type with different specifications can be placed horizontally at the same time.
  • the heat exchange sheet there are flow guiding fins between the corner holes and various types and sizes of heat exchange fins.
  • the placement of the guide fins can be placed according to the flow requirements of the heat exchange medium.
  • the heat exchange fins on the heat exchange plates in all heat exchange layers are laterally disposed. That is, in the heat exchanger, various types and various specifications of heat exchange fins are arranged in a horizontal row in different fluid layers faced by different heat exchange mediums.
  • At least one heat exchange fin in the heat exchange layer through which the heat exchange medium flows is arranged in a row. That is, in the heat exchanger, in the different fluid layers faced by different heat exchange medium, some heat transfer fins in the fluid layer are taken in a horizontal arrangement, and some heat exchange fins in the fluid layer The film is still in a traditional placement.
  • FIG. 1 is a schematic view showing the outline of a sealless plate fin heat exchanger of the present invention
  • Figure 2 is a schematic view showing the first structure of the heat exchanger sheet in the present invention
  • Figure 3 is a top plan view of the C-C section of Figure 2
  • Figure 4 is a schematic view showing the second structure of the heat exchanger sheet in the present invention.
  • FIG. 5 is a third structural schematic view of the heat exchange sheet of the present invention.
  • FIG. 6 is a fourth structural diagram of the heat exchange sheet of the present invention.
  • Figure 7 is a fifth structural schematic view of the heat exchange sheet of the present invention.
  • Figure 8 is a sixth structural schematic view of the heat exchange sheet of the present invention.
  • FIG. 9 is a seventh structural view of the heat exchange sheet of the present invention.
  • Figure 10 is a schematic view of the eighth structure of the heat exchanger sheet in the present invention.
  • FIG 11 is a ninth structural schematic view of the heat exchange sheet of the present invention.
  • Figure 12 is a tenth structural view of the heat exchange sheet of the present invention
  • Fig. 1 is a schematic diagram of the horizontal arrangement of the serrated fins and the flow direction of the heat exchange medium.
  • Fig. 14 is a schematic view of the horizontal arrangement of the flat perforated fins and the flow direction of the heat exchange medium.
  • FIG. 1 shows the outer structure of a sealless plate fin heat exchanger, and a sealless plate fin heat exchanger includes a heat exchange plate 1 having a peripheral bevel seal, an outer baffle 2 and a tube. Mouth 3.
  • FIG. 2 shows a structural schematic view of the heat exchange plate 1 and the fins, including the corner hole 6, the peripheral sealing slope 5, which is disposed laterally in the heat exchange region on the heat exchange plate 1.
  • the serrated type heat exchange fins 9, two angular holes 6 are respectively disposed on the low plane 4 and the high plane 7, and the height between the low plane 4 and the high plane 7 is equal to the height of the heat exchange fins 9.
  • Guide vanes 8 are provided in the region surrounded by the edges of the low plane 4, the high plane 7 and the serrated heat exchange fins 9, and the height of the guide fins 8 is the same as the height of the fins 9.
  • Fig. 3 is a schematic plan view of the C-C section of Fig. 2, showing the sealing bevel 5 of the heat exchange sheet 1 and the sawtooth type heat exchange fins 9.
  • FIG. 4 Another structure of the heat exchanger sheet 1 and the fins is shown in Fig. 4, and the differences between Fig. 4 and Fig. 2 are shown.
  • the serration type heat exchange fins 10 and the sawtooth type heat exchange fins 9 have different specifications, in particular, different pitches.
  • the heat exchange sheet 1 of Figures 4 and 2 and the fins having different specifications are disposed in the same heat exchanger, indicating two adjacent heat exchange fluid layers when the two heat exchange mediums exchange heat with each other. A number of heat exchange plates 1 and various fins will form a combination of heat exchange layers.
  • FIG. 5 shows still another structure of the heat exchange sheet 1 and the fins, and FIG. 5 and FIG. 2 are different in that the heat exchange area on the heat exchange sheet 1 is laterally disposed.
  • FIG. 6 shows still another structure of the heat exchange sheet 1 and the corner hole sealing form, and FIG. 6 and FIG. 5 are different in that the two corner holes 6 are used for the heat exchange medium mutual
  • the sealed plane is provided with a joint seal block 12 having a thickness equal to the height of the flat perforated heat exchange fins 11.
  • Fig. 7 shows still another structure of the heat exchange sheet 1 and the fins
  • Fig. 7 and Fig. 6 differ in that heat exchange in the heat exchange region on the heat exchange sheet 1
  • the type of the fins is different.
  • a schematic diagram of a sawtooth type heat exchange fin 9 is shown in Fig. 7, and the thickness of the joint seal block 12 is the same as the height of the sawtooth type heat exchange fin 9.
  • FIG. 8 another structure of the heat exchange sheet 1 and the fins is shown in Fig. 8.
  • the difference between Fig. 8 and Fig. 7 is that there is a sawtooth type change in the heat exchange region on the heat exchange sheet.
  • the heat fins 10, and one of the corner holes 6 are provided with flow guiding fins 8, and the thickness of the joint sealing block 12 is the same as the height of the flow guiding fins 8 and the height of the sawtooth type heat exchange fins 10.
  • FIG. 9 shows still another structure of the heat exchange sheet 1 and the corner hole sealing form, and FIG. 9 and FIG. 7 are different in that one of the corner holes 6 is provided with a sealing ring 13 .
  • the thickness of the seal ring 13 is equal to the height of the sawtooth type heat exchange fins 9.
  • FIG. 10 another structure of the heat exchange sheet 1 and the fins is shown in Fig. 10.
  • the difference between Fig. 10 and Fig. 4 is that the horizontal rows are simultaneously arranged in the heat exchange region of the heat exchange sheet 1.
  • Placed with serrations A type of heat exchange fin 9 or 10 and a horizontally perforated type of heat exchange fin 11 placed horizontally.
  • Fig. 11 shows still another structure of the heat exchange sheet 1 and the fins
  • Fig. 11 and Fig. 10 are different in that the heat exchange sheets 1 are simultaneously horizontally arranged in the heat exchange region.
  • Heat exchange fins 9 or 10 of a sawtooth type and heat exchange fins 9 or 10 of a sawtooth type are placed in a row.
  • FIG. 12 another structure of the heat exchange sheet 1 and the fins is shown in Fig. 12, and Fig. 12 and Fig. 10 are different in that the heat exchange region of the heat exchange sheet 1 is simultaneously horizontally
  • the row is provided with a heat exchange fin 9 or 10 of a sawtooth type and a heat exchange fin 11 of a straight perforation type placed in a row.
  • FIG. 12 is a schematic view showing the arrangement of the sawtooth type heat exchange fins 9 or 10 and the flow direction of the heat exchange medium, the undulation extending direction 15 of the heat exchange fins 9 or 10, and the heat exchange medium in the heat exchanger.
  • the overall flow direction is 14 parallel.
  • FIG. 13 is a schematic view showing the horizontal arrangement of the horizontally-punched type heat exchange fins 11 and the flow direction of the heat exchange medium, the undulation extending direction 15 of the heat exchange fins 11 and the overall heat exchange medium in the heat exchanger.
  • the flow direction is parallel.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

一种无封条板翅式换热器
技术领域
本发明涉及一种换热器领域， 特别涉及一种无封条板翅式换热器。 背景技术
.在传统无封条板翅式换热器中，翅片在换热板片内放置的方式都是以翅 片的节距断截面迎合换热介质， 形成一种翅片顺排的放置方式，使换热介质 可以顺畅的流过翅片并进行换热。 例如专利号 20061 0039927. 1 和专利号 02828683. 9在其说明书附图中所表示的翅片放置形式。
在传统无封条板翅式换热器中，翅片的这种顺排放置方式其换热效率较 低， 为了满足介质流体的换热要求一般采用多加换热板片和翅片的方法， 最 后将造成产品的体积和重量较大， 成本较高。
在传统无封条板翅式换热器中，翅片的这种顺排放置方式往往不能满足 某些介质的换热要求，尤其不能满足冷媒这类在换热过程中会发生相变的介 质进行换热的要求，使得这类换热形式在传统无封条板翅式换热器中的应用 受到了局限。
发明内容
本发明的目的就是针对现有技术中存在的上述问题，提供一种换热效率 高， 体积和重量较小， 成本低， 可以满足具有相变性质的介质进行换热的无 封条板翅式换热器。
实现本发明目的的技术方案是： 一种无封条板翅式换热器， 包括外挡 板、 管嘴、 若干设有翅片的换热板片和周边密封斜面， 其特征是， 在所述若 干设有翅片的换热板片中，至少有一个换热介质流通层面上的换热翅片横向 设置。
所述换热板片上的换热翅片横向设置是指换热翅片的起伏延伸方向和 换热器内换热介质的总体流向平行。
本发明中通过改变换热翅片的放置方向，将换热翅片的传统放置方向平 面旋转 90° ， 使换热翅片的节距断截面与换热器内换热介质的总休流向平 行， 形成一种换热翅片横排的放置方式， 换热介盾在换热翅片内被翅片的凸 起部分所阻拦和干扰，使换热介质在通过翅片上的切口或通过翅片上的小孔 后被强迫短距离横向流动，换热介质在各换热层面横排放置的翅片内形成连 续 S形状的流动趋势， 目的是在换热介质流体阻力允许的前提下，加大各种 换热介质在翅片和换热板片之间的换热效率，以此减少换热板片和换热翅片 的数量， 减少产品的体积和重量以及成本， 并以此满足具有相变性质的介质 进行换热的要求。
实现本发明目的技术方案后的无封条板翅式换热器主要可用于蒸发器 和冷凝器以及其它的换热环境中，尤其适用于制冷行业中各种冷媒这种具有 两相性质的介质进行换热。
在传统无封条板翅式换热器中， 现存在许多角孔密封的形式； 有的角 孔密封方式采用板材液压方式，使角孔周边用于换热介质相互密封的平面分 别设在低平面和高平面上，低平面与高平面之间的高度等于所述换热翅片的 高度。有的角孔密封方式采用在角孔周边用于换热介质相互密封的平面上设 有连体密封块， 连体密封块的厚度等于所述换热翅片的高度。有的角孔密封 方式采用在单个角孔周边用于换热介质相互密封的平面上设有角孔密封环， 密封环的厚度等于所述换热翅片的高度。
在传统无封条板翅式换热器中， 大部分均为两种介质的相互换热， 但 是也有在一台无封条板翅式换热器内有三种介质相对换热的形式。
在传统无封条板翅式换热器中，有的采用换热介质对角流的换热方式， 有的釆用换热介质同边流的换热方式。
在传统无封条板翅式换热器中， 有的换热板片采用表面复合有低熔点 焊料的板材， 而换热翅片的材料为一般箔材， 翅片材料上没有低熔点焊料。 在传统无封条板翅式换热器中， 有的换热板片采用表面无焊料的一般 板材， 但是在换热翅片的箔材上复合有低熔点焊料。
在传统无封条板翅式换热器中， 有的换热板片采用表面无焊料的一般 板材，换热翅片的材料表面也为没复合有低熔点焊料的一般箔材，但是在换 热板片与换热翅片之间加有箔状的低熔, 焊料。
在无封条板翅式换热器中， 无论角孔釆用何种密封方式， 无论在一台 换热器中是两种或三种介质相互换热， 无论采用对角流或同边流的换热方 式， 以及无论低熔点焊料采用何种添加方式， 均可在换热板片的换热区域内 将翅片横排放置， 实现本发明的技术方案。
作为本发明的进一步改进，所述换热翅片包括有各种规格的锯齿类型换 热翅片和平直打孔类型换热翅片。
作为本发明的进一步改进， 在同一台换热器内， 在两种以上换热介质所 对应的两个以上流体层面中，各流体层面分别对应于同一种规格的换热翅片 或不同规格的换热翅片。 即在同一台换热器内， 不同换热介质所对应的不同. 流体层面可以采用相同规格的换热翅片， 也可以采用不同规格的换热翅片。 换热翅片的规格一般是指翅片的高度、材料厚度和节距等，针对锯齿类型的 换热翅片， 其规格还包括切口长度等参数。 针对平直打孔类型的换热翅片， 其规格还包括打孔的孔径和孔距等参数。
作为本发明的进一步改进， 在同一个换热器内， 在两种以上换热介质所 对应的两个以上流体层面中，各流体层面分别对应于同一种类型的换热翅片 或不同类型的换热翅片。 即在同一台换热器内， 不同换热介质所对应的不同 流体层面可以采用同一种类型的换热翅片，同时还可以是同种规格或不同规 格的换热翅片， 也可以采用不同类型的换热翅片。
作为本发明的进一步改进， 在同一台换热器内， 至少有一个换热介盾 流通层面的每一块换热板片上，同时横排放置具有不同规格或不同类型的换 热翅片组合。 即在同一台换热器内， 在不同换热介质所对应的不同流体层面 中， 至少在流通某一种换热介质的每一块换热板片上， 可以同时横排放置具 有不同规格的锯齿类型换热翅片和平直打孔类型的换热翅片。
作为本发明的进一步改进， 在同一个换热器内， 至少有一个换热介质 流通层面的每一块换热板片上，同时横排和顺排放置具有不同规格或不同类 型的换热翅片组合。 即在同一台换热器内，在不同换热介质所对应的不同流 体层面中， 至少在流通某一种换热介质的每一块换热板片上， 可以同时横排 放置具有不同规格的锯齿类型换热翅片和顺排放置具有不同规格的平直打 孔类型换热翅片，或同时顺排放置具有不同规格的锯齿类型换热翅片和横排 ,放置具有不同规格的平直打孔类型换热翅片，
作为本发明的进一步改进， 在换热板片上， 在角孔与各种类型、 各种 规格的换热翅片之间有导流翅片。导流翅片的放置形式可按换热介质的流动 要求进行摆放。
作为本发明的进一步改进，所有换热层面内换热板片上的换热翅片均 为横向设置。即在所述换热器内，在不同换热介质所面对的不同流体层面内， 各种类型及各种规格的换热翅片均采用横排的放置方式。
作为本发明的进一步改进， 在所有换热层面内的换热板片上， 在不同 .换热介质中 ,还至少有一种换热介质所流通的换热层面内的换热翅片采用顺 排设置。 即在所述换热器内， 在不同换热介质所面对的不同流体层面内， 有 的流体层面内的换热翅片釆取横排的放置方式，有的流体层面内的换热翅片 仍采用传统的顺排放置方式。
附图说明
图 1是本发明无封条板翅式换热器外形示意图
图 2是本发明中换热板片的第一种结构示意图 图 3是图 2的 C- C剖面俯视示意图
图 4是本发明中换热板片的第二种结构示意图
图 5是本发明中换热板片的第三种结构示意图
图 6是本发明中换热板片的第四种结构示意图
图 7是本发明中换热板片的第五种结构示意图
图 8是本发明中换热板片的第六种结构示意图
图 9是本发明中换热板片的第七种结构示意图
图 1 0是本发明中换热板片的第八种结构示意图
图 11是本发明中换热板片的第九种结构示意图
图 12是本发明中换热板片的第十种结构示意图
图 1 3是锯齿类型翅片横排放置方式示意以及换热介质流向示意图 图 14是平直打孔类型翅片横排放置方式以及换热介质流向示意图 具体实施方式
下面结合附图对本发明做进一步说明。
如图 1所示， 图 1中显示了无封条板翅式换热器外形结构， 一种无封条 板翅式换热器包括具有周边斜面密封的换热板片 1， 外挡板 2和管嘴 3。
如图 2所示， 图 2中显示了换热板片 1和翅片的一种结构示意图， 包括 角孔 6、 周边密封斜面 5 , 在换热板片 1上的换热区域内横向设置的锯齿类 型换热翅片 9， 两个角孔 6分别设在低平面 4和高平面 7上， 低平面 4与高 平面 7之间的高度等于换热翅片 9的高度。 在低平面 4、 高平面 7和锯齿类 型换热翅片 9的边缘围成的区域内设有导流翅片 8 , 导流翅片 8的高度与翅 片 9的高度相同。
如图 3所示， 图 3是图 2的 C-C剖面俯视示意图， 显示出了换热板片 1 周边的密封斜面 5和锯齿类型换热翅片 9的示意。
图 4中显示了换热板片 1和翅片的另一种结构，图 4和图 2的不同之处 在于， 在换热板片 1上的换热区域内， 锯齿类型换热翅片 10与锯齿类型换 热翅片 9的规格不同， 尤其是节距不同。 图 4和图 2中的换热板片 1和具有 不同规格的翅片设在同一台换热器的中，表示两种换热介质进行相互换热时 两个相邻的换热流体层面。若干换热板片 1以及各种翅片将构成各换热层面 的组合。
如图 5所示， 图 5中显示了换热板片 1和翅片的再一种结构， 图 5和图 2的不同之处在于， 在换热板片 1上的换热区域内横向设置有平直打孔类型 的换热翅片 1 1。
如图 6所示， 图 6中显示了换热板片 1和角孔密封形式的再一种结构， 图 6和图 5的不同之处在于，两个角孔 6周边用于换热介质相互密封的平面 上设有连体密封块 12， 连体密封块 12的厚度与平直打孔换热翅片 11的高 度相同。
如图 7所示， 图 7中显示了换热板片 1和翅片的再一种结构， 图 7和图 6的不同之处在于， 在换热板片 1上的换热区域内换热翅片的类型不同.， 在 图 7中表示了一种锯齿类型换热翅片 9的示意， 连体密封块 12的厚度与锯 齿类型换热翅片 9的高度相同。
如图 8所示， 图 8中显示了换热板片 1和翅片的再一种结构， 图 8和图 7的不同之处在于， 在换热板片上的换热区域内有锯齿类型换热翅片 10 , 以 及其中一个角孔 6带有导流翅片 8 , 连体密封块 12的厚度与导流翅片 8的 高度和锯齿类型换热翅片 10的高度相同。
如图 9所示， 图 9中显示了换热板片 1和角孔密封形式的再一种结构， 图 9和图 7的不同之处在于， 其中一个角孔 6设有密封环 1 3 , 密封环 13的 厚度等于锯齿类型换热翅片 9的高度。
如图 10所示， 图 10中显示了换热板片 1和翅片的再一种结构， 图 10 和图 4的不同之处在于，在换热板片 1的换热区域内同时横排放置有锯齿类 型的换热翅片 9或 10和横排放置的平直打孔类型的换热翅片 11。
如图 11所示， 图 11中显示了换热板片 1和翅片的再一种结构， 图 11 和图 10的不同之处在于， 在换热板片 1的换热区域内同时横排放置有锯齿 类型的换热翅片 9或 10和顺排放置有锯齿类型的换热翅片 9或 10。
如图 12所示， 图 12中显示了换热板片 1和翅片的再一种结构， 图 12 ,和图 10的不同之处在于， 在换热板片 1的换热区域内同时横排放置有锯齿 类型的换热翅片 9或 10和顺排放置有平直打孔类型的换热翅片 11。
如图 13所示， 图 12是锯齿类型换热翅片 9或 10横排放置示意以及换 热介质流向示意图，换热翅片 9或 10的起伏延伸方向 15和换热器内换热介 质的总体流向 14平行。
如图 14所示， 图 13是平直打孔类型换热翅片 11横排放置示意以及换 热介质流向示意图，换热翅片 11的起伏延伸方向 15和换热器内换热介质的 总体流向 14平行。

Claims

权 利 要 求
1、 一种无封条板翅式换热器， 包括外挡板、 管嘴、 若干设有翅片的换热 板片和周边密封斜面， 其特征是，在所述若干设有翅片的换热板片中， 至少有一个换热介质流通层面的换热板片上带有横向设置的换热翅 片。
2、 根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 所述换热 翅片包括锯齿类型换热翅片。
3、 根据权利要求 1或 2所述的无封条板翅式换热器， 其特征在于， 所述 换热翅片包括平直打孔类型换热翅片。
4、 根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 在两种以 上换热介质所对应的两个以上流体层面中， 各流体层面分别对应于一 种类型的换热翅片。
5、 根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 在两种以 上换热介质所对应的两个以上流体层面中， 各流体层面分别对应于不 同类型的换热翅片。
6、 根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 至少一个 换热介质流通层面内所述的换热板片上设有两种以上类型的横排的换 热翅片。
7、 根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 至少一个 换热介质流通层面内所述的换热板片上设有横排设置和顺排设置的换 热翅片。
8、 根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 所述翅片 横向设置的换热板片上带有导流翅片。
9、 根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 所有换热 层面内换热板片上的换热翅片均为横向设置。
根据权利要求 1所述的无封条板翅式换热器， 其特征在于， 在两个以 上换热层面内的换热板片上， 至少有一种换热介质所流通的换热层面 内的换热翅片采用顺排设置。
PCT/CN2008/000011 2007-06-12 2008-01-02 Échangeur thermique de type à plaques-ailettes sans bande d'étanchéité WO2008151497A1 (fr)

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JP2010511473A JP2010529408A (ja) 2007-06-12 2008-01-02 シールストリップなしのプレートフィン式熱交換
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CN101071051A (zh) 2007-11-14
EP2172728A1 (en) 2010-04-07
CN100516758C (zh) 2009-07-22
EP2172728A4 (en) 2013-01-16
DK2172728T3 (en) 2019-02-25
EP2172728B1 (en) 2018-11-28
JP2010529408A (ja) 2010-08-26
US9453685B2 (en) 2016-09-27
US20100175858A1 (en) 2010-07-15

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