TW202122737A - Heat exchanger - Google Patents

Heat exchanger Download PDF

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TW202122737A
TW202122737A TW108144299A TW108144299A TW202122737A TW 202122737 A TW202122737 A TW 202122737A TW 108144299 A TW108144299 A TW 108144299A TW 108144299 A TW108144299 A TW 108144299A TW 202122737 A TW202122737 A TW 202122737A
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Taiwan
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heat exchanger
fins
fluid
long side
fluid collection
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TW108144299A
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Chinese (zh)
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TWI727533B (en
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宋柏毅
徐仲彥
林志忠
林育立
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財團法人工業技術研究院
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Priority to TW108144299A priority Critical patent/TWI727533B/en
Priority to CN201911288358.8A priority patent/CN112902725A/en
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Publication of TWI727533B publication Critical patent/TWI727533B/en
Publication of TW202122737A publication Critical patent/TW202122737A/en

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    • 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
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0015—Heat and mass exchangers, e.g. with permeable walls

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Cooling Or The Like Of Electrical Apparatus (AREA)

Abstract

A heat exchanger is provided. The heat exchanger includes a fluid inlet disposed on an end of a long side of the heat exchanger; a fluid outlet disposed on another end of the long side of the heat exchanger; a plurality of spacer plates respectively disposed on the long side, on another long side, and between the long side and the another long side; a plurality of fins, disposed among the plurality of spacer plates; and a plurality of fluid confluence structures, formed on the plurality of fins along a direction of an inlet flow and an outlet flow and the spacer plates between the long side and the another side.

Description

熱交換器Heat exchanger

本案係有關於一種熱交換器。This case is related to a heat exchanger.

現在工業的製程中，為了將工廠製程中所排放出的廢熱重新利用，通常會加裝熱交換器將熱能從廢氣中取出，並將熱能轉換至其他需要使用的地方。傳統所使用的熱交換器主要係以鋁擠(aluminum extrusion)的方式製造，並由熱管、複數個鰭片、中央隔板與殼體所組成。熱交換器的設計通常係將複數個鰭片及中央隔板等距設置，並在殼體之長邊面開設冷水口及出水口，以達到解熱的效果。In the current industrial process, in order to reuse the waste heat emitted from the factory process, a heat exchanger is usually installed to remove the heat energy from the exhaust gas and convert the heat energy to other places where it needs to be used. Traditionally used heat exchangers are mainly manufactured by aluminum extrusion, and are composed of heat pipes, a plurality of fins, a central partition and a shell. The design of the heat exchanger is usually to equidistantly arrange a plurality of fins and a central partition, and to open a cold water outlet and a water outlet on the long side of the shell to achieve the effect of heat dissipation.

第1a圖係傳統熱交換器之內部流場分析，由此圖可以看出，傳統熱交換器之流速較快的區域係集中在靠近冷水口及出水口的區域，再由第1b圖的傳統熱交換器的內部溫度分析可以知道，在遠離冷水口及出水口的區域與靠近冷水口及出水口的區域有明顯溫差變化，此表示傳統交換器的內部流體不均勻，進而會降低次系統內的模組的發電總量。Figure 1a is an analysis of the internal flow field of a traditional heat exchanger. From this figure, it can be seen that the area with a faster flow rate of the traditional heat exchanger is concentrated in the area near the cold water outlet and the water outlet. The internal temperature analysis of the heat exchanger shows that there is a significant temperature difference between the area far away from the cold water outlet and water outlet and the area near the cold water outlet and water outlet. This indicates that the internal fluid of the traditional exchanger is not uniform, which will reduce the temperature in the secondary system. The total power generation of the modules.

因此，本案提供一種可透過簡易加工程序製作之熱交換器，並且此熱交換器能夠使內部流場達到均溫化(homoeothermic)的效果。Therefore, the present application provides a heat exchanger that can be manufactured through a simple processing procedure, and the heat exchanger can achieve the homoeothermic effect of the internal flow field.

有鑑於此，本案係提供一種熱交換器，熱交換器包含：流體入口，其係設置在熱交換器之長側邊之一端；流體出口，其係設置在熱交換器之長側邊之另一端；複數個隔板，其係配置在熱交換器之長側邊、另一長側邊，以及長側邊與另一長側邊之間；複數個鰭片，係配置在複數個隔板之間；以及複數個流體匯集結構，其係沿著一流體的一流入方向以及流體的一流出方向形成在複數個鰭片上以及複數個隔板中配置在長側邊與該另一長側邊之間之該些隔板。In view of this, the present case provides a heat exchanger. The heat exchanger includes: a fluid inlet, which is arranged on one end of the long side of the heat exchanger; and a fluid outlet, which is arranged on the other of the long side of the heat exchanger. One end; a plurality of baffles, which are arranged on the long side of the heat exchanger, the other long side, and between the long side and the other long side; a plurality of fins are arranged on the plurality of baffles Between; and a plurality of fluid collection structures, which are formed on a plurality of fins along a fluid inflow direction and a fluid outflow direction, and a plurality of partitions are arranged on the long side and the other long side Between these partitions.

為讓本案能更明顯易懂，下文特舉實施例，並配合所附圖式作詳細說明如下。In order to make this case more obvious and easy to understand, the following specific examples are given in conjunction with the accompanying drawings for detailed descriptions as follows.

以下藉由特定的具體實施例說明本案之實施方式，熟習此項技藝之人士可由本文所揭示之內容輕易地瞭解本案之其他優點及功效。須知，本說明書所附圖式所繪示之結構、比例、大小等，均僅用以配合說明書所揭示之內容，以供熟悉此技藝之人士之瞭解與閱讀，並非用以限定本案可實施之限定條件，故不具技術上之實質意義，任何結構之修飾、比例關係之改變或大小之調整，在不影響本案所能產生之功效及所能達成之目的下，均應仍落在本案所揭示之技術內容得能涵蓋之範圍內。The following specific examples are used to illustrate the implementation of this case. Those who are familiar with this technique can easily understand the other advantages and effects of this case from the content disclosed in this article. It should be noted that the structure, proportion, size, etc. shown in the accompanying drawings in this manual are only used to match the contents disclosed in the manual for the understanding and reading of those familiar with the art, and are not used to limit the implementation of this case. Limited conditions, so it does not have technical substantive significance. Any structural modification, proportional relationship change or size adjustment, without affecting the effect and the purpose that can be achieved in this case, should still fall within the disclosure of this case The technical content must be able to cover the scope.

請參閱第2a圖及第2b圖，第2a圖及第2b圖分別為本案一實施例之熱交換器1之立體圖以及該立體圖之A-A’剖面圖。熱交換器1係與一熱源(未示於圖式)貼合。此處雖敘述為貼合，但不侷限於此，凡熱交換器及熱源間能夠達成熱量傳遞的連接方式皆適用於本案之熱交換器。為了能夠達成良好的熱傳導效應以及製造上簡便，本案之熱交換器選用的材質為鋁材，但不侷限於此材料。Please refer to Fig. 2a and Fig. 2b. Fig. 2a and Fig. 2b are respectively a perspective view of the heat exchanger 1 according to an embodiment of the present invention and a cross-sectional view A-A' of the perspective view. The heat exchanger 1 is attached to a heat source (not shown in the drawings). Although it is described as bonding here, it is not limited to this. Any connection method that can achieve heat transfer between the heat exchanger and the heat source is applicable to the heat exchanger in this case. In order to achieve a good heat conduction effect and ease of manufacture, the heat exchanger in this case is made of aluminum, but it is not limited to this material.

在一實施例中，本案之熱交換器1包含：流體入口11，其係設置在熱交換器1之長側邊10a之一端。流體出口12，其係設置在熱交換器1之長側邊10a之另一端。熱交換器1所使用的流體為冷水。熱交換器1更包含有複數個隔板13，其係配置在熱交換器1之該長側邊10a、另一長側邊10b，以及長側邊10a與另一長側邊10b之間。在一實施例中，複數個隔板13間的間距係相等。在一實施例中，流體入口11及流體出口12分別朝流體的流入方向L1以及流體的流出方向L2貫穿設置於長側邊10a之隔板13。In one embodiment, the heat exchanger 1 of this case includes: a fluid inlet 11 which is disposed at one end of the long side 10a of the heat exchanger 1. The fluid outlet 12 is arranged at the other end of the long side 10a of the heat exchanger 1. The fluid used in the heat exchanger 1 is cold water. The heat exchanger 1 further includes a plurality of partitions 13 which are arranged between the long side 10a, the other long side 10b, and the long side 10a and the other long side 10b of the heat exchanger 1. In one embodiment, the spacing between the plurality of partitions 13 is equal. In an embodiment, the fluid inlet 11 and the fluid outlet 12 respectively penetrate the partition 13 provided on the long side 10a toward the fluid inflow direction L1 and the fluid outflow direction L2.

請參閱第2a圖及第2b圖，在一實施例中，熱交換器1包括複數個鰭片14，複數個鰭片14係配置在複數個隔板13之間。在一實施例中，隔板13與鰭片以及鰭片與鰭片之間的距離係相等，並且鰭片14沿著流體的流入方向L1(或流體的流出方向L2)設置。複數個隔板13之厚度係大於該複數個鰭片14之厚度。在一實施例中，複數個隔板13與複數個鰭片14係一體成形。Please refer to FIGS. 2a and 2b. In one embodiment, the heat exchanger 1 includes a plurality of fins 14, and the plurality of fins 14 are arranged between the plurality of partitions 13. In an embodiment, the distance between the partition 13 and the fin and the distance between the fin and the fin is equal, and the fin 14 is arranged along the inflow direction L1 of the fluid (or the outflow direction L2 of the fluid). The thickness of the plurality of partitions 13 is greater than the thickness of the plurality of fins 14. In one embodiment, the plurality of partitions 13 and the plurality of fins 14 are integrally formed.

在一實施例中，複數個鰭片14與複數個隔板13係以等距排列設置。In one embodiment, the plurality of fins 14 and the plurality of partitions 13 are arranged in an equidistant arrangement.

請參照第2b圖，在一實施例中，複數個鰭片14包含複數個結構鰭片14a以及複數個散熱鰭片14b。複數個結構鰭片14a間隔設置在複數個隔板13之間，並且係等距設置。在另一實施例中，複數個結構鰭片14a係與熱交換器1之上表面10e以及下表面10f連接。複數個散熱鰭片14b中，有的散熱鰭片14b係設置於隔板13與結構鰭片14a之間，以及有的散熱鰭片14b係設置於兩相鄰結構鰭片14a之間。在另一實施例中，複數個散熱鰭片14b係與熱交換器1之上表面10e或下表面10f之一者連接。在一實施例中，單一結構鰭片14a之高度係大於單一散熱鰭片14b之高度。在另一實施例中，單一結構鰭片14a之高度係與單一隔板13之高度相同。也就是說，這些結構鰭片14a給予熱交換器1應有之高度及結構強度，這些散熱鰭片14b使熱交換器1之內部流場的內壓力平衡，提升流場均勻性。Please refer to FIG. 2b. In one embodiment, the plurality of fins 14 includes a plurality of structural fins 14a and a plurality of heat dissipation fins 14b. The plurality of structural fins 14a are arranged at intervals between the plurality of partitions 13 and are arranged at equal intervals. In another embodiment, a plurality of structural fins 14a are connected to the upper surface 10e and the lower surface 10f of the heat exchanger 1. Among the plurality of heat dissipation fins 14b, some heat dissipation fins 14b are arranged between the partition plate 13 and the structural fins 14a, and some heat dissipation fins 14b are arranged between two adjacent structural fins 14a. In another embodiment, a plurality of heat dissipation fins 14b are connected to one of the upper surface 10e or the lower surface 10f of the heat exchanger 1. In one embodiment, the height of the single structure fin 14a is greater than the height of the single heat dissipation fin 14b. In another embodiment, the height of the single structure fin 14a is the same as the height of the single partition 13. In other words, these structural fins 14a give the heat exchanger 1 the desired height and structural strength, and these heat dissipation fins 14b balance the internal pressure of the internal flow field of the heat exchanger 1 and improve the uniformity of the flow field.

請參照第3a圖及第3b圖之本案熱交換器之B-B’橫切面圖，其中第3b圖是第3a圖之局部的一放大圖。在一實施例中，熱交換器包括複數個流體匯集結構15，複數個流體匯集結構15沿著一流體的流入方向L1以及該流體的流出方向L2形成在複數個鰭片14上並且配置在長側邊10a與另一長側邊10b之間的隔板13。在一實施例中，流體匯集結構15係貫穿複數個鰭片14並且配置在長側邊10a與另一長側邊10b之間的該些隔板13的孔洞。Please refer to Figure 3a and Figure 3b of the B-B' cross-sectional view of the heat exchanger of this case, where Figure 3b is an enlarged view of a part of Figure 3a. In one embodiment, the heat exchanger includes a plurality of fluid collection structures 15, which are formed on a plurality of fins 14 along the inflow direction L1 of a fluid and the outflow direction L2 of the fluid, and are arranged on the long The partition 13 between the side 10a and the other long side 10b. In one embodiment, the fluid collection structure 15 penetrates through the plurality of fins 14 and is arranged in the holes of the partitions 13 between the long side 10a and the other long side 10b.

請參照第3b圖，在一實施例中，複數個流體匯集結構15包括複數個前半部流體匯集結構15a以及複數個後半部流體匯集結構15b。在一實施例中，複數個前半部流體匯集結構15a係形成於熱交換器1之配置在長側邊10a之隔板13以及中間位置之該些隔板13之間的複數個鰭片14。在一實施例中，複數個後半部流體匯集結構15b係形成於設置在熱交換器1之中間位置之該些隔板13以及配置在熱交換器1之另一長側邊10b之該些隔板13與配置在熱交換器1之中間位置之該些隔板13間的複數個鰭片14。在一實施例中，複數個流體匯集結構15係沿著流體流入方向L1以及流體流出方向L2形成。Referring to FIG. 3b, in one embodiment, the plurality of fluid collection structures 15 include a plurality of front-half fluid collection structures 15a and a plurality of back-half fluid collection structures 15b. In one embodiment, a plurality of front-half fluid collection structures 15a are formed on the plurality of fins 14 between the partitions 13 arranged on the long sides 10a of the heat exchanger 1 and the partitions 13 in the middle position. In one embodiment, a plurality of rear-half fluid collecting structures 15b are formed on the partitions 13 arranged in the middle of the heat exchanger 1 and the partitions arranged on the other long side 10b of the heat exchanger 1. The plate 13 and a plurality of fins 14 arranged between the partition plates 13 in the middle of the heat exchanger 1. In one embodiment, a plurality of fluid collection structures 15 are formed along the fluid inflow direction L1 and the fluid outflow direction L2.

在另一實施例中，複數個後半部流體匯集結構15b中的單一流體匯集結構15b之孔徑係大於複數個前半部流體匯集結構15a中的單一流體匯集結構15之孔徑。複數個流體匯集結構15係為圓形孔洞或是橢圓形孔洞。本案熱交換器1之流體匯集結構15並不侷限於圓形或橢圓形，亦可為其他形狀之通孔。本案中，後半部與前半部流體匯集結構之孔徑也可稱為寬度。In another embodiment, the pore size of the single fluid collection structure 15b of the plurality of rear-half fluid collection structures 15b is larger than the pore size of the single fluid collection structure 15 of the plurality of front-half fluid collection structures 15a. The plurality of fluid collection structures 15 are circular holes or elliptical holes. The fluid collection structure 15 of the heat exchanger 1 in this case is not limited to a circular or elliptical shape, and may be a through hole of other shapes. In this case, the aperture of the fluid collection structure in the rear half and the front half can also be referred to as the width.

另一實施例中，複數個後半部流體匯集結構15b係根據複數個前半部流體匯集結構15a之孔洞以偏移擴孔(offset reaming)的方式形成。複數個前半部流體匯集結構15a中的單一流體匯集結構之孔徑係相同於流體入口11以及流體出口12之孔徑。In another embodiment, the plurality of rear-half fluid collection structures 15b are formed by offset reaming according to the holes of the plurality of front-half fluid collection structures 15a. The pore size of the single fluid collection structure in the plurality of front-half fluid collection structures 15a is the same as the pore size of the fluid inlet 11 and the fluid outlet 12.

請參考第4a圖至第4e圖，第4a圖為本案之熱交換器之縱向切面圖，其中Y為散熱鰭片的高度。第4b-1圖及第4b-2圖為本案之不同高度之散熱鰭片14b之流場及溫度場模擬分析。當Y=16mm時，此時散熱鰭片14b之高度與結構鰭片14a以及隔板13之高度相同，意即，散熱鰭片14b係與熱交換器1之上表面10e以及下表面10f連接。此狀態可視為散熱鰭片將流道完全分隔。如第4b-1圖及第4b-2圖所示，流體進入熱交換器1後，由於鰭片14的高度一致而導致流體無法順暢地流入熱交換器1之後半部，流體在熱交換器1的前半部快速流通，因此熱交換器1後半部的熱量無法被有效地解除，高溫顯示在流體流入方向L1之深處；當Y=0mm時，此狀態可視為沒有設置散熱鰭片14b。如第4c-1圖及第4c-2圖所示，流體進入熱交換器1中後，由於沒有散熱鰭片14b，流體在熱交換1的前半段呈現均勻的，但從溫度圖來看，熱交換器1之後半部的熱量仍無法被有效解除；當Y=11mm時，如第4d-1圖及第4d-2圖所示，流體均勻地流入各鰭片14之間以及鰭片14與隔板13之間，由溫度分布圖亦可發現流體在熱交換器1中的溫度較趨近於一致，沒有過高之區域。在一實施例中，散熱鰭片的高度係至少高於結構鰭片的高度的一半。Please refer to Fig. 4a to Fig. 4e. Fig. 4a is a longitudinal section view of the heat exchanger in this case, where Y is the height of the fins. Fig. 4b-1 and Fig. 4b-2 show the simulation analysis of the flow field and temperature field of the heat dissipation fins 14b of different heights. When Y=16mm, the height of the heat dissipation fin 14b is the same as the height of the structural fin 14a and the partition 13 at this time, which means that the heat dissipation fin 14b is connected to the upper surface 10e and the lower surface 10f of the heat exchanger 1. This state can be regarded as a complete separation of the runners by the cooling fins. As shown in Figures 4b-1 and 4b-2, after the fluid enters the heat exchanger 1, the height of the fins 14 is the same, so that the fluid cannot flow smoothly into the back half of the heat exchanger 1. The front half of 1 circulates quickly, so the heat in the second half of the heat exchanger 1 cannot be effectively relieved. The high temperature is displayed in the depth of the fluid inflow direction L1; when Y=0mm, this state can be regarded as no cooling fins 14b. As shown in Figures 4c-1 and 4c-2, after the fluid enters the heat exchanger 1, since there is no heat dissipation fin 14b, the fluid appears uniform in the first half of the heat exchange 1, but from the temperature diagram, The heat in the rear half of the heat exchanger 1 still cannot be effectively relieved; when Y=11mm, as shown in Figures 4d-1 and 4d-2, the fluid flows evenly between the fins 14 and the fins 14 It can also be found from the temperature distribution graph that the temperature of the fluid in the heat exchanger 1 is closer to the same with the partition plate 13, and there is no excessively high area. In one embodiment, the height of the heat dissipation fins is at least higher than half of the height of the structural fins.

請參考第4e圖，第4e圖為散熱鰭片高度與解熱量之關係圖。綜上所述，當散熱鰭片隨高度增加時，其解熱量也會跟著上升，均溫的效果也會更明顯；然而，在未裝設散熱鰭片以及完全分隔流道的狀態下，解熱量將明顯地下降，且無法達到均溫的效果。Please refer to Figure 4e. Figure 4e shows the relationship between the height of the cooling fins and the amount of heat. In summary, when the heat dissipation fins increase in height, their heat dissipation will also increase, and the effect of uniform temperature will be more obvious; however, when the heat dissipation fins are not installed and the flow channel is completely separated, the solution The heat will drop significantly, and the effect of uniform temperature cannot be achieved.

請參考第5a圖至第5e圖，第5a圖為第3b圖之上視圖，X1為前半部流體匯集結構之寬度，X2為後半部流體匯集結構之寬度，當散熱鰭片的高度在11mm時，根據不同的流體匯集結構的寬度差，即X2-X1，其解熱效果也會有差異。請參考第5b-1圖及第5b-2圖，第5b-1圖及第5b-2圖係在寬度差為0 mm時，分別為熱交換器1之流場分布圖以及溫度分布圖。在寬度差為0 mm的情況下，意即，前半部流體匯集結構之寬度與後半部流體匯集結構之寬度相同，由流場分布圖可以發現，流體無法有效地進入到熱交換器1後半部之深處，由溫度分布圖亦可以發現相對高溫集中在流體的流入方向之深處；請參照第5c-1圖及第5c-2圖，在寬度差為19.05 mm的情況下，由於孔徑差過大，可以發現流體進入後可以直接流通至熱交換器1之後半部，但在熱交換器1之中段出現相對較低的流速，由溫度分布圖也可得知在熱交換器1中段的溫度偏高；請參照第5d-1圖及第5d-2圖，在寬度差為6.35 mm的情況下，從流場分布圖中，可以發現流場在整體熱交換器1的分布更為均勻，而在溫度的分布上也趨為均勻。Please refer to Figures 5a to 5e, Figure 5a is the top view of Figure 3b, X1 is the width of the front half of the fluid collection structure, X2 is the width of the back half of the fluid collection structure, when the height of the fins is 11mm , According to the width difference of different fluid collection structure, namely X2-X1, its antipyretic effect will also be different. Please refer to Figures 5b-1 and 5b-2. Figures 5b-1 and 5b-2 are the flow field distribution diagram and temperature distribution diagram of heat exchanger 1 when the width difference is 0 mm. When the width difference is 0 mm, it means that the width of the front half of the fluid collection structure is the same as the width of the second half of the fluid collection structure. From the flow field distribution diagram, it can be found that the fluid cannot effectively enter the back half of the heat exchanger 1 From the temperature distribution diagram, it can also be found that the relatively high temperature is concentrated in the depth of the inflow direction of the fluid; please refer to Figure 5c-1 and Figure 5c-2. When the width difference is 19.05 mm, due to the difference in aperture If it is too large, it can be found that the fluid can directly circulate to the back half of heat exchanger 1 after entering, but a relatively low flow rate appears in the middle section of heat exchanger 1. The temperature distribution chart also shows that the temperature in the middle section of heat exchanger 1 Too high; please refer to Figure 5d-1 and Figure 5d-2. When the width difference is 6.35 mm, from the flow field distribution diagram, it can be found that the flow field is more evenly distributed in the overall heat exchanger 1. And the temperature distribution also tends to be uniform.

請參考第5e圖，第5e圖為流體匯集口的寬度差與解熱量之關係圖。在一實施例中，複數個後半部流體匯集結構之孔徑係大於等於複數個前半部流體匯集結構之孔徑的兩倍，且小於等於複數個前半部流體匯集結構之孔徑的三倍。綜上所述，前半部流體匯集結構之寬度與後半部流體匯集結構之寬度相同或是在寬度差過大的情況下，以本實施例來說，在寬度差為15.87 mm以上時，流場及溫度場的分布分別在熱交換器1之後半部及中段處較為不均勻，而在寬度差在上述兩者之間時，流場及溫度場的分布趨勢也呈現更均勻，也因此可以得到較佳之解熱量。Please refer to Figure 5e. Figure 5e shows the relationship between the width difference of the fluid collection port and the amount of heat removal. In one embodiment, the pore size of the plurality of back-half fluid collection structures is greater than or equal to twice the pore size of the plurality of front-half fluid collection structures, and less than or equal to three times the pore size of the plurality of front-half fluid collection structures. In summary, the width of the front half of the fluid collection structure is the same as the width of the second half of the fluid collection structure or when the width difference is too large. In this embodiment, when the width difference is 15.87 mm or more, the flow field and The distribution of the temperature field is relatively uneven in the back half and the middle section of the heat exchanger 1, and when the width difference is between the above two, the distribution trend of the flow field and temperature field is also more uniform, so it can be more uniform. The best solution for calories.

本案之熱交換器藉由散熱鰭片與結構鰭片具有高度差的設計，並且搭配前半部流體匯集結構之寬度與後半部流體匯集結構之寬度具有寬度差的設計，來達成熱交換器在操作時使內部流場以及溫度場能夠達成均勻的功效，因而使熱交換器之內部的流體解熱量提升。The heat exchanger in this case is designed with a height difference between the heat dissipation fins and the structural fins, and the width of the front half of the fluid collection structure and the width of the second half of the fluid collection structure have a width difference to achieve the operation of the heat exchanger. At this time, the internal flow field and temperature field can achieve a uniform effect, thereby increasing the amount of fluid decomposing inside the heat exchanger.

然本案以實施例已揭露如上，然其並非用以限定本案，任何所屬技術領域中具有通常知識者，在不脫離本案之精神和範圍內，當可作些許之更動與潤飾，故本案之保護範圍當視後附之申請專利範圍所界定者為準。Although this case has been disclosed as above by the example, it is not used to limit the case. Anyone with ordinary knowledge in the technical field can make some changes and modifications without departing from the spirit and scope of the case. Therefore, the protection of this case The scope shall be subject to the definition of the attached patent application scope.

1:熱交換器 10a:長側邊 10b:另一長側邊 10e:上表面 10f:下表面 11:流體入口 12:流體出口 13:隔板 14:鰭片 14a:結構鰭片 14b:散熱鰭片 15:流體匯集結構 15a:前半部流體匯集結構 15b:後半部流體匯集結構 L1:流體的流入方向 L2:流體的流出方向 X1:前半部流體匯集結構之寬度 X2:後半部流體匯集結構之寬度 Y:散熱鰭片的高度1: Heat exchanger 10a: Long side 10b: the other long side 10e: upper surface 10f: bottom surface 11: fluid inlet 12: fluid outlet 13: partition 14: Fins 14a: Structural fins 14b: cooling fins 15: Fluid collection structure 15a: Front half fluid collection structure 15b: The fluid collection structure of the second half L1: Inflow direction of fluid L2: Outflow direction of fluid X1: The width of the front half of the fluid collection structure X2: The width of the back half of the fluid collection structure Y: The height of the cooling fins

第1a圖係傳統熱交換器的內部流場分布圖。 第1b圖係傳統熱交換器的內部溫度分布圖。 第2a圖係本案一實施例之熱交換器之立體圖。 第2b圖係本案一實施例之熱交換器之立體圖之A-A’剖面圖。 第3a圖係本案熱交換器之B-B’橫切面圖。 第3b圖係本案熱交換器之B-B’橫切面圖之局部放大圖。 第4a圖係本案另一實施例之熱交換器之A-A’剖面圖。 第4b-1圖及第4b-2圖係分別為散熱鰭片高度Y=16 mm之流場分布圖以及溫度場分布圖。 第4c-1圖及第4c-2圖係分別為散熱鰭片高度Y=0 mm之流場分布圖以及溫度場分布圖。 第4d-1圖及第4d-2圖係分別為散熱鰭片高度Y=11 mm之流場分布圖以及溫度場分布圖。 第4e圖為散熱鰭片高度與解熱量之關係圖。 第5a圖係第3b圖之上視圖。 第5b-1圖及第5b-2圖係分別為寬度差為0 mm時的熱交換器之流場分布圖以及溫度分布圖。 第5c-1圖及第5c-2圖係分別為寬度差為19.05 mm時的熱交換器之流場分布圖以及溫度分布圖。 第5d-1圖及第5d-2圖係分別為寬度差為6.35 mm時的熱交換器流場分布圖以及溫度分布圖。 第5e圖為匯集口寬度差與解熱量之關係圖。Figure 1a is the internal flow field distribution diagram of a conventional heat exchanger. Figure 1b shows the internal temperature distribution of a conventional heat exchanger. Figure 2a is a perspective view of the heat exchanger of an embodiment of the present invention. Figure 2b is an A-A' cross-sectional view of a perspective view of the heat exchanger according to an embodiment of the present invention. Figure 3a is a B-B' cross-sectional view of the heat exchanger in this case. Figure 3b is a partial enlarged view of the B-B' cross-sectional view of the heat exchanger in this case. Figure 4a is a cross-sectional view of the heat exchanger A-A' of another embodiment of the present invention. Figure 4b-1 and Figure 4b-2 are the flow field distribution diagram and the temperature field distribution diagram with the height of the fins Y=16 mm, respectively. Figure 4c-1 and Figure 4c-2 are respectively the flow field distribution diagram and the temperature field distribution diagram with the height of the fins Y=0 mm. Figure 4d-1 and Figure 4d-2 are the flow field distribution diagram and the temperature field distribution diagram with the fin height Y=11 mm, respectively. Figure 4e shows the relationship between the height of the cooling fins and the amount of heat. Figure 5a is a top view of Figure 3b. Figure 5b-1 and Figure 5b-2 are the flow field distribution diagram and temperature distribution diagram of the heat exchanger when the width difference is 0 mm, respectively. Figure 5c-1 and Figure 5c-2 are respectively the flow field distribution diagram and temperature distribution diagram of the heat exchanger when the width difference is 19.05 mm. Figure 5d-1 and Figure 5d-2 are the flow field distribution diagram and temperature distribution diagram of the heat exchanger when the width difference is 6.35 mm, respectively. Figure 5e is a graph showing the relationship between the difference in the width of the collection port and the amount of heat.

11:流體入口11: fluid inlet

13:隔板13: partition

14:鰭片14: Fins

14a:結構鰭片14a: Structural fins

14b:散熱鰭片14b: cooling fins

15:流體匯集結構15: Fluid collection structure

15a:前半部流體匯集結構15a: Front half fluid collection structure

15b:後半部流體匯集結構15b: The fluid collection structure of the second half

Claims (10)

一種熱交換器，包括： 一流體入口，設置在該熱交換器之一長側邊之一端； 一流體出口，設置在該熱交換器之該長側邊之另一端； 複數個隔板，配置在該熱交換器之該長側邊、另一長側邊，以及該長側邊與該另一長側邊之間； 複數個鰭片，配置在該複數個隔板之間；以及 複數個流體匯集結構，其係沿著一流體之流入方向以及該流體之流出方向形成在該複數個鰭片上以及該複數個隔板中配置在該長側邊與該另一長側邊之間之該些隔板上。A heat exchanger, including: A fluid inlet arranged at one end of one long side of the heat exchanger; A fluid outlet provided at the other end of the long side of the heat exchanger; A plurality of baffles are arranged on the long side, the other long side, and between the long side and the other long side of the heat exchanger; A plurality of fins are arranged between the plurality of partitions; and A plurality of fluid collection structures are formed on the plurality of fins along the inflow direction of a fluid and the outflow direction of the fluid, and the plurality of partitions are arranged between the long side and the other long side It's on these partitions. 如申請專利範圍第1項所述的熱交換器，其中該複數個鰭片與該複數個隔板係以等距排列設置。The heat exchanger according to item 1 of the scope of patent application, wherein the plurality of fins and the plurality of baffles are arranged in an equidistant arrangement. 如申請專利範圍第1項所述的熱交換器，其中該些鰭片係包含複數個結構鰭片以及複數個散熱鰭片，該複數個結構鰭片之單一結構鰭片的高度係大於該複數個散熱鰭片之單一散熱鰭片的高度。The heat exchanger according to claim 1, wherein the fins include a plurality of structural fins and a plurality of heat dissipation fins, and the height of a single structure fin of the plurality of structural fins is greater than the plurality of fins The height of a single cooling fin of each cooling fin. 如申請專利範圍第3項所述的熱交換器，其中該單一散熱鰭片的高度係至少高於該單一結構鰭片的高度的一半。The heat exchanger according to claim 3, wherein the height of the single heat dissipation fin is at least higher than half of the height of the single structure fin. 如申請專利範圍第3項所述的熱交換器，其中該複數個結構鰭片之單一結構鰭片的高度與該複數個隔板之單一隔板的高度相同。The heat exchanger according to item 3 of the scope of patent application, wherein the height of the single structure fin of the plurality of structure fins is the same as the height of the single partition of the plurality of partitions. 如申請專利範圍第1項所述的熱交換器，其中該複數個流體匯集結構包括複數個前半部流體匯集結構以及複數個後半部流體匯集結構，該複數個前半部流體匯集結構係形成於在該熱交換器之該長側邊之該些隔板以及配置在該熱交換器之中間之該些隔板之間的該些鰭片，該複數個後半部流體匯集結構係形成於該熱交換器之間之該些隔板以及配置在該熱交換器之該另一長側邊之該些隔板與配置在熱交換器之中間位置之該些隔板間的該些鰭片，該複數個後半部流體匯集結構中的單一流體匯集結構之孔徑係大於該複數個前半部流體匯集結構中的單一流體匯集結構之孔徑。The heat exchanger according to item 1 of the patent application, wherein the plurality of fluid collection structures include a plurality of front-half fluid collection structures and a plurality of back-half fluid collection structures, and the plurality of front-half fluid collection structures are formed in The baffles on the long side of the heat exchanger and the fins arranged between the baffles in the middle of the heat exchanger, and the plurality of back-half fluid collecting structures are formed in the heat exchange The partitions between the heat exchangers and the partitions arranged on the other long side of the heat exchanger and the fins between the partitions arranged in the middle of the heat exchanger, the plural The pore size of the single fluid collection structure in the second half fluid collection structure is larger than the pore size of the single fluid collection structure in the plurality of front half fluid collection structures. 如申請專利範圍第6項所述的熱交換器，其中該複數個流體匯集結構係圓形或是橢圓形孔洞。The heat exchanger according to item 6 of the scope of patent application, wherein the plurality of fluid collecting structures are circular or elliptical holes. 如申請專利範圍第6項所述的熱交換器，其中該複數個後半部流體匯集結構係以偏移擴孔的方式形成。According to the heat exchanger described in item 6 of the scope of the patent application, the plurality of rear-half fluid collecting structures are formed in a manner of offset reaming. 如申請專利範圍第6項所述的熱交換器，其中該複數個前半部流體匯集結構中的單一流體匯集結構之孔徑係相同於該流體入口之孔徑。According to the heat exchanger described in item 6 of the scope of patent application, the pore size of the single fluid collection structure in the plurality of front-half fluid collection structures is the same as that of the fluid inlet. 如申請專利範圍第6項所述的熱交換器，其中該複數個後半部流體匯集結構之孔徑係大於等於該複數個前半部流體匯集結構之孔徑的兩倍，且小於等於該複數個前半部流體匯集結構之孔徑的三倍。The heat exchanger described in item 6 of the scope of patent application, wherein the pore diameters of the plurality of back-half fluid collecting structures are greater than or equal to twice the pore diameter of the plurality of front-half fluid collecting structures, and less than or equal to the plurality of front halves Three times the pore size of the fluid collection structure.
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