CN220491966U - Battery pack - Google Patents
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- CN220491966U CN220491966U CN202321827183.5U CN202321827183U CN220491966U CN 220491966 U CN220491966 U CN 220491966U CN 202321827183 U CN202321827183 U CN 202321827183U CN 220491966 U CN220491966 U CN 220491966U
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Abstract
本实用新型涉及电池技术领域,公开了一种电池包,包括电池和换热板,换热板与电池相贴合,换热板包括多个沿第一方向间隔设置的换热介质通道,换热板沿第二方向的相对两端分别设有换热介质入口和换热介质出口,其中,第一方向与第二方向相交,换热介质通道包括第一流道和出液流道,换热介质入口、第一流道、出液流道以及换热介质出口沿第一方向依次连通;多个出液流道的总流通面积大于多个第一流道的总流通面积。本实用新型的电池包,通过设置多个出液流道的总流通面积大于第一流道的总流通面积,以解决换热效果不均匀的问题。
The utility model relates to the field of battery technology and discloses a battery pack, which includes a battery and a heat exchange plate. The heat exchange plate is attached to the battery. The heat exchange plate includes a plurality of heat exchange medium channels spaced apart along a first direction. The opposite ends of the hot plate along the second direction are respectively provided with a heat exchange medium inlet and a heat exchange medium outlet, wherein the first direction intersects with the second direction, and the heat exchange medium channel includes a first flow channel and a liquid outlet flow channel. The medium inlet, the first flow channel, the liquid outlet flow channel and the heat exchange medium outlet are sequentially connected along the first direction; the total flow area of the plurality of liquid outlet flow channels is greater than the total flow area of the plurality of first flow channels. The battery pack of the present invention solves the problem of uneven heat exchange effect by arranging multiple liquid outlet flow channels with a total flow area larger than the total flow area of the first flow channel.
Description
技术领域Technical field
本实用新型涉及电池技术领域,特别是涉及一种电池包。The utility model relates to the field of battery technology, in particular to a battery pack.
背景技术Background technique
热管理是根据具体对象的要求,利用加热或冷却手段对其温度或温差进行调节和控制的过程。电池包在充电或放电时会释放一定能量,因此,需要对电池包进行冷却。电池包在低温环境中,电池包的电解液黏稠,导致电池包内的锂电池的内阻增加,加上负极材料极化严重,造成锂离子沉积、镀膜现象等,将使锂电池使可用容量、放电速率下降,锂离子电池会随着温度的降低,所能释放的能量是在减少的,而且容量在减少、电压也变低,最终电池续航力大减。因此,需要对电池包进行加热。对电池包进行降温或加热为电池包的热管理。其中,在电池包中通常设置换热板,将电池与换热板相贴,在换热板中设置换热介质通道,在换热介质通道中充入换热介质,以实现对电池进行冷却或加热进而达到对电池热管理的目的。换热板是热管理部件的关键。Thermal management is a process that uses heating or cooling means to adjust and control the temperature or temperature difference of a specific object according to the requirements of the object. The battery pack releases a certain amount of energy when charging or discharging, so the battery pack needs to be cooled. When the battery pack is in a low-temperature environment, the electrolyte of the battery pack becomes viscous, which causes the internal resistance of the lithium battery in the battery pack to increase. In addition, the negative electrode material is seriously polarized, causing lithium ion deposition and coating phenomena, which will reduce the available capacity of the lithium battery. , The discharge rate decreases. As the temperature of the lithium-ion battery decreases, the energy it can release decreases, the capacity decreases, the voltage becomes lower, and ultimately the battery life is greatly reduced. Therefore, the battery pack needs to be heated. Cooling or heating the battery pack is the thermal management of the battery pack. Among them, a heat exchange plate is usually provided in the battery pack, the battery is attached to the heat exchange plate, a heat exchange medium channel is provided in the heat exchange plate, and the heat exchange medium is filled into the heat exchange medium channel to cool the battery. Or heating to achieve the purpose of battery thermal management. Heat exchange plates are the key to thermal management components.
现有地换热板从换热介质入口到换热介质出口的换热介质通道设计均一,换热介质在换热介质通道内的流动距离越长,换热介质的温度变化越大,换热能力越差,因此,沿换热介质的流动方向,位于流动方向末端的换热介质对电池的热管理效果明显变差,进而导致电池的热管理效果不均匀,不利于电池的性能稳定和使用寿命。The existing heat exchange plate has a uniform heat exchange medium channel design from the heat exchange medium inlet to the heat exchange medium outlet. The longer the flow distance of the heat exchange medium in the heat exchange medium channel, the greater the temperature change of the heat exchange medium. Therefore, along the flow direction of the heat exchange medium, the thermal management effect of the heat exchange medium at the end of the flow direction on the battery becomes significantly worse, which in turn leads to uneven thermal management effect of the battery, which is not conducive to the stable performance and use of the battery. life.
实用新型内容Utility model content
本实用新型的目的是提供一种电池包,以解决现有电池包中的换热板流道结构不合理,热管理效果不均的问题。The purpose of this utility model is to provide a battery pack to solve the problems of unreasonable flow channel structure of the heat exchange plate and uneven thermal management effect in the existing battery pack.
为了实现上述目的,本实用新型提供了一种电池包,包括电池和换热板,所述换热板与所述电池相贴合,In order to achieve the above purpose, the present utility model provides a battery pack, which includes a battery and a heat exchange plate, and the heat exchange plate is attached to the battery.
所述换热板包括至少一个换热介质通道,多个所述换热介质通道沿第一方向间隔设置,所述换热板沿第二方向的相对两端分别设有换热介质入口和换热介质出口,其中,所述第一方向与所述第二方向相交,所述换热介质通道包括第一流道和第二流道,所述换热介质入口、所述第一流道、所述第二流道以及所述换热介质出口沿所述第二方向依次连通;The heat exchange plate includes at least one heat exchange medium channel. A plurality of the heat exchange medium channels are spaced apart along the first direction. The opposite ends of the heat exchange plate along the second direction are respectively provided with a heat exchange medium inlet and an exchange medium channel. Heat medium outlet, wherein the first direction intersects the second direction, the heat exchange medium channel includes a first flow channel and a second flow channel, the heat exchange medium inlet, the first flow channel, the The second flow channel and the heat exchange medium outlet are sequentially connected along the second direction;
多个所述第二流道的总流通面积大于所述第一流道的总流通面积。The total flow area of the plurality of second flow channels is greater than the total flow area of the first flow channels.
优选的,每个所述换热介质通道包括一个所述第一流道和多个所述第二流道,相邻的两个所述第二流道沿所述第一方向间隔设置,所述第一流道与多个所述第二流道连通。Preferably, each of the heat exchange medium channels includes one first flow channel and a plurality of second flow channels, and two adjacent second flow channels are spaced apart along the first direction. The first flow channel communicates with a plurality of second flow channels.
优选的,每个所述第二流道沿所述第二方向包括多个子流段,每个所述子流段包括多个子流道,在第二方向上相邻的两个所述子流段的子流道相连通,所述子流段的所述子流道的数量沿所述第二方向朝向所述换热介质出口的一端逐段增加,所述子流段的总流通面积沿所述第二方向朝向所述换热介质出口的一端逐段增加。Preferably, each second flow channel includes a plurality of sub-flow sections along the second direction, each of the sub-flow sections includes a plurality of sub-flow channels, and two adjacent sub-flow sections in the second direction The sub-flow channels of the sub-flow segments are connected, the number of the sub-flow channels of the sub-flow segments increases segment by segment along the second direction toward one end of the heat exchange medium outlet, and the total flow area of the sub-flow segments is along the The second direction increases gradually toward one end of the heat exchange medium outlet.
优选的,所述子流段的其中一个所述子流道与靠近所述换热介质出口的相邻的所述子流段中的多个所述子流道连通。Preferably, one of the sub-flow channels in the sub-flow section is connected to a plurality of the sub-flow channels in the adjacent sub-flow sections close to the heat exchange medium outlet.
优选的,多个所述子流道的宽度沿所述第二方向逐段减小,多个所述子流道在所述第一方向之间的间距沿所述第二方向逐段减小。Preferably, the width of the plurality of sub-flow channels decreases step by step along the second direction, and the spacing between the plurality of sub-flow channels in the first direction decreases step by step along the second direction. .
优选的,相邻的两个所述第二流道在第一方向之间的间距小于相邻的两个所述第一流道在所述第一方向之间的间距。Preferably, the distance between two adjacent second flow channels in the first direction is smaller than the distance between two adjacent first flow channels in the first direction.
优选的,所述换热板沿第二方向的相对两端分别设有沿所述第一方向延伸的换热介质流入槽和换热介质流出槽,多个所述第一流道通过所述换热介质流入槽与所述换热介质入口连通,多个所述第二流道通过所述换热介质流出槽与所述换热介质出口连通。Preferably, opposite ends of the heat exchange plate along the second direction are respectively provided with heat exchange medium inflow grooves and heat exchange medium outflow grooves extending along the first direction, and a plurality of the first flow channels pass through the exchanger. The heat medium inflow groove is connected to the heat exchange medium inlet, and the plurality of second flow channels are connected to the heat exchange medium outlet through the heat exchange medium outflow groove.
优选的,所述换热板包括盖板和基板,所述盖板与所述基板密封连接形成所述换热板,所述盖板设有所述换热介质通道,或Preferably, the heat exchange plate includes a cover plate and a base plate, the cover plate and the base plate are sealingly connected to form the heat exchange plate, and the cover plate is provided with the heat exchange medium channel, or
所述基板设有所述换热介质通道,或The substrate is provided with the heat exchange medium channel, or
所述基板与所述盖板的相对面分别设有所述换热介质通道。The heat exchange medium channels are respectively provided on the opposite surfaces of the base plate and the cover plate.
优选的,所述换热介质通道的高度h在第三方向上占所述换热板的总厚度H的50%-75%。Preferably, the height h of the heat exchange medium channel accounts for 50%-75% of the total thickness H of the heat exchange plate in the third direction.
优选的,所述换热板还包括第一接头和第二接头,所述第一接头通过所述换热介质入口与所述第一流道连通,所述第二接头通过所述换热介质出口与所述第二流道连通。Preferably, the heat exchange plate further includes a first joint and a second joint, the first joint is connected to the first flow channel through the heat exchange medium inlet, and the second joint is connected through the heat exchange medium outlet. connected to the second flow channel.
优选的,还包括箱体,所述箱体具有容纳腔,所述电池和所述换热板均设于所述容纳腔内;或Preferably, it also includes a box body, the box body has a receiving cavity, and the battery and the heat exchange plate are both located in the receiving cavity; or
框体,所述框体和所述换热板共同限定出容纳腔,所述电池设于所述容纳腔内。A frame body, the frame body and the heat exchange plate jointly define an accommodation cavity, and the battery is disposed in the accommodation cavity.
本实用新型提供一种电池包,与现有技术相比,其有益效果在于:电池包包括电池和换热板,换热板与电池相贴合,由于换热板中具有换热介质,换热板与电池相贴合,电池与换热板中的换热介质发生热交换,以实现对电池包的热管理。换热板包括至少一个换热介质通道,换热板沿第二方向的相对两端分别设有换热介质入口和换热介质出口,换热介质入口用于换热介质的进入,换热介质出口用于换热介质的流出,换热介质在换热介质入口进入换热介质通道,换热介质在换热介质通道中与电池进行热交换后,通过换热介质出口排出换热板,换热介质通过换热介质入口、换热介质通道以及换热介质出口实现换热介质的流动循环,换热介质入口与换热介质出口在第二方向上的相对两端设置,以保证换热介质通道在第二方向上的热管理覆盖面积,使电池在第二方向上均有换热介质通道的布置,保证电池在第二方向上的热管理效果,换热介质通道包括第一流道和第二流道,换热介质入口、第一流道、第二流道以及换热介质出口沿第二方向依次连通,换热介质从换热介质入口进入第一流道,从第一流道进入第二流道后再从换热介质出口流出换热板,以形成完整的换热介质通道路径,换热介质通过换热介质通道路径实现换热介质的循环。多个第二流道的总流通面积大于第一流道的总流通面积。在换热介质从换热介质入口进入第一流道,此时换热介质与电池的热交换较少,因此,换热介质在第一流道中的热管理效果较好。当换热介质经过第一流道后,在第一流道中与电池进行部分热交换后,导致进入第二流道的换热介质的热交换能力下降,通过增大第二流道的总流通面积,使第二流道的总流通面积大于第一流道的总流通面积,增大第二流道的吸热面积,提升第二流道中的换热介质的吸热能力,进而解决换热介质通道在换热介质入口端与换热介质出口端的热管理效果差异大的技术问题,使换热板在第二方向上的整体热管理效果均匀,对电池整体的热管理效果更均匀。The utility model provides a battery pack. Compared with the prior art, the beneficial effect is that the battery pack includes a battery and a heat exchange plate. The heat exchange plate is attached to the battery. Since the heat exchange plate has a heat exchange medium, the heat exchange plate can The hot plate is attached to the battery, and heat exchange occurs between the battery and the heat exchange medium in the heat exchange plate to achieve thermal management of the battery pack. The heat exchange plate includes at least one heat exchange medium channel. Opposite ends of the heat exchange plate along the second direction are respectively provided with a heat exchange medium inlet and a heat exchange medium outlet. The heat exchange medium inlet is used for the entry of the heat exchange medium. The heat exchange medium The outlet is used for the outflow of the heat exchange medium. The heat exchange medium enters the heat exchange medium channel at the heat exchange medium inlet. After heat exchange with the battery in the heat exchange medium channel, the heat exchange medium is discharged from the heat exchange plate through the heat exchange medium outlet. The heat medium realizes flow circulation of the heat exchange medium through the heat exchange medium inlet, the heat exchange medium channel and the heat exchange medium outlet. The heat exchange medium inlet and the heat exchange medium outlet are arranged at opposite ends in the second direction to ensure that the heat exchange medium The thermal management coverage area of the channel in the second direction enables the battery to have a heat exchange medium channel arrangement in the second direction to ensure the thermal management effect of the battery in the second direction. The heat exchange medium channel includes a first flow channel and a third flow channel. The two flow channels, the heat exchange medium inlet, the first flow channel, the second flow channel and the heat exchange medium outlet are connected in sequence along the second direction. The heat exchange medium enters the first flow channel from the heat exchange medium inlet and enters the second flow channel from the first flow channel. After the passage, the heat exchange plate flows out from the heat exchange medium outlet to form a complete heat exchange medium channel path, and the heat exchange medium realizes the circulation of the heat exchange medium through the heat exchange medium channel path. The total flow area of the plurality of second flow channels is greater than the total flow area of the first flow channels. When the heat exchange medium enters the first flow channel from the heat exchange medium inlet, there is less heat exchange between the heat exchange medium and the battery. Therefore, the heat management effect of the heat exchange medium in the first flow channel is better. When the heat exchange medium passes through the first flow channel and performs partial heat exchange with the battery in the first flow channel, the heat exchange capacity of the heat exchange medium entering the second flow channel decreases. By increasing the total flow area of the second flow channel, Make the total flow area of the second flow channel larger than the total flow area of the first flow channel, increase the heat absorption area of the second flow channel, and improve the heat absorption capacity of the heat exchange medium in the second flow channel, thereby solving the problem of the heat exchange medium channel. The technical problem of the large difference in thermal management effect between the inlet end of the heat exchange medium and the outlet end of the heat exchange medium makes the overall thermal management effect of the heat exchange plate in the second direction uniform, and the overall thermal management effect of the battery is more uniform.
附图说明Description of the drawings
图1为本实用新型实施例的整体结构示意图。Figure 1 is a schematic diagram of the overall structure of an embodiment of the present utility model.
图2为本实用新型实施例换热板的爆炸结构图。Figure 2 is an exploded structural view of the heat exchange plate according to the embodiment of the present utility model.
图3为本实用新型实施例基板的结构示意图图。Figure 3 is a schematic structural diagram of a substrate according to an embodiment of the present invention.
图4为本实用新型实施例换热介质通道的结构示意图。Figure 4 is a schematic structural diagram of the heat exchange medium channel according to the embodiment of the present invention.
图5为本实用新型的图3中的A-A处的剖面图;Figure 5 is a cross-sectional view of the utility model at A-A in Figure 3;
图6为本实用新型的图3中的B-B处的剖面图;Figure 6 is a cross-sectional view of the utility model at B-B in Figure 3;
图7为本实用新型的图5中的C处的放大结构示意图;Figure 7 is an enlarged structural schematic diagram of position C in Figure 5 of the present invention;
图8为本实用新型的图6中的D处的放大结构示意图;Figure 8 is an enlarged structural schematic diagram of D in Figure 6 of the present invention;
图9为本实用新型的图5与图6的结构对比图;Figure 9 is a structural comparison diagram of Figures 5 and 6 of the present utility model;
图10为本实用新型实施例盖板的结构示意图。Figure 10 is a schematic structural diagram of the cover plate according to the embodiment of the present invention.
图11为本实用新型实施例基板的内部结构剖视图。Figure 11 is a cross-sectional view of the internal structure of the substrate according to the embodiment of the present invention.
图12为本实用新型实施例图6中的A处放大结构示意图。Figure 12 is an enlarged structural schematic diagram of position A in Figure 6 according to the embodiment of the present invention.
图中:In the picture:
100、换热板;200、电池;100. Heat exchange plate; 200. Battery;
1、盖板;11、换热介质入口;12、换热介质出口;1. Cover plate; 11. Heat exchange medium inlet; 12. Heat exchange medium outlet;
2、基板;20、换热介质通道;201、第一流道;202、第二流道;2021、子流段;2022、子流道;21、换热介质流入槽;22、换热介质流出槽2. Base plate; 20. Heat exchange medium channel; 201. First flow channel; 202. Second flow channel; 2021. Sub-flow section; 2022. Sub-flow channel; 21. Heat exchange medium inflow tank; 22. Heat exchange medium outflow groove
3、第一接头;4、第二接头;3. The first connector; 4. The second connector;
X、第一方向;Y、第二方向;Z、第二方向。X, first direction; Y, second direction; Z, second direction.
具体实施方式Detailed ways
下面将结合本申请实施例中的附图,对本申请实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本申请的一部分实施例,而不是全部的实施例。The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present application. Obviously, the described embodiments are only some of the embodiments of the present application, rather than all of the embodiments.
请一并参阅图1至图12,本实用新型实施例提供一种电池包,包括电池200和换热板100,换热板100与电池200相贴合,需要说明的是换热板100可以与电池200的一侧相贴合,也可以与电池200的多侧相贴合,由于换热板100中可通入换热介质,换热板100与电池200相贴合,换热介质在换热板100内流过后电池200与换热板100进行热交换,以实现对电池200的热管理。Please refer to Figures 1 to 12 together. An embodiment of the present invention provides a battery pack, which includes a battery 200 and a heat exchange plate 100. The heat exchange plate 100 is attached to the battery 200. It should be noted that the heat exchange plate 100 can It can be attached to one side of the battery 200, or can also be attached to multiple sides of the battery 200. Since the heat exchange medium can be passed into the heat exchange plate 100, the heat exchange plate 100 is attached to the battery 200, and the heat exchange medium is in After flowing through the heat exchange plate 100, the battery 200 performs heat exchange with the heat exchange plate 100 to achieve thermal management of the battery 200.
如图2至图3所示,换热板100包括至少一个换热介质通道20,其中,换热介质通道20为多个时,相邻的两个换热介质通道20沿第一方向X间隔设置。多个换热介质通道20在第一方向X间隔设置,以使换热介质通道20在换热板100的第一方向X的热交换覆盖面积更大,提升在第一方向X上对电池200的热管理效果。换热板100沿第二方向Y的相对两端分别设有换热介质入口11和换热介质出口12,换热介质入口11用于换热介质的进入,换热介质出口12用于换热介质的流出,换热介质在换热介质入口11进入换热介质通道20,在换热介质通道20与电池200进行热交换后,通过换热介质出口12排出换热板100,换热介质通过换热介质入口11、换热介质通道20以及换热介质出口12实现换热介质的循环流动,换热介质入口11与换热介质出口12在第二方向Y上的相对两端设置,以保证换热介质通道20在第二方向Y上的换热介质的覆盖面积,使电池200在第二方向Y上均有换热介质通道20的布置,保证电池200在第二方向Y上的热管理效果,换热介质通道20包括第一流道201和第二流道202,换热介质入口11、第一流道201、第二流道202以及换热介质出口12沿第二方向Y依次连通,换热介质从换热介质入口11第一流道201,并从第一流道201进入第二流道202后,再从换热介质出口12流出换热板100,以形成完整的换热介质通道路径,换热介质通过换热介质通道路径实现换热介质的循环。其中,第一方向X与第二方向Y相交,在第一方向X上有多个换热介质通道20的间隔设置,在第二方向Y上具有换热介质通道20的延伸,在两个方向上均保证电池200的热管理效果,提升电池200的热管理能力。As shown in FIGS. 2 to 3 , the heat exchange plate 100 includes at least one heat exchange medium channel 20 . When there are multiple heat exchange medium channels 20 , two adjacent heat exchange medium channels 20 are spaced apart along the first direction X. set up. A plurality of heat exchange medium channels 20 are arranged at intervals in the first direction X, so that the heat exchange coverage area of the heat exchange medium channels 20 in the first direction thermal management effect. The opposite ends of the heat exchange plate 100 along the second direction Y are respectively provided with a heat exchange medium inlet 11 and a heat exchange medium outlet 12. The heat exchange medium inlet 11 is used for the entry of heat exchange medium, and the heat exchange medium outlet 12 is used for heat exchange. When the medium flows out, the heat exchange medium enters the heat exchange medium channel 20 at the heat exchange medium inlet 11. After heat exchange between the heat exchange medium channel 20 and the battery 200, it is discharged from the heat exchange plate 100 through the heat exchange medium outlet 12. The heat exchange medium passes through The heat exchange medium inlet 11, the heat exchange medium channel 20 and the heat exchange medium outlet 12 realize the circulation flow of the heat exchange medium. The heat exchange medium inlet 11 and the heat exchange medium outlet 12 are arranged at opposite ends in the second direction Y to ensure that The coverage area of the heat exchange medium of the heat exchange medium channel 20 in the second direction Y enables the battery 200 to have the heat exchange medium channel 20 arranged in the second direction Y, ensuring thermal management of the battery 200 in the second direction Y. As a result, the heat exchange medium channel 20 includes a first flow channel 201 and a second flow channel 202. The heat exchange medium inlet 11, the first flow channel 201, the second flow channel 202 and the heat exchange medium outlet 12 are connected in sequence along the second direction Y. The heat medium enters the first flow channel 201 from the heat exchange medium inlet 11 and enters the second flow channel 202 from the first flow channel 201, and then flows out of the heat exchange plate 100 from the heat exchange medium outlet 12 to form a complete heat exchange medium channel path. The heat exchange medium realizes the circulation of the heat exchange medium through the heat exchange medium channel path. Wherein, the first direction X and the second direction Y intersect, there are a plurality of heat exchange medium channels 20 arranged at intervals in the first direction All of the above ensure the thermal management effect of the battery 200 and improve the thermal management capability of the battery 200.
如图2至图3所示,多个第二流道202的总流通面积大于第一流道201的总流通面积。当第一流道201为多个时,多个第二流道202的总流通面积大于多个第一流道201的总流通面积。其中,图5为图3中的A-A处的剖面图,以展示在在第一方向X上间隔设置有多个第一流道201,且在图中标出多个第一流道201的流通面积,其中,第一流道201的总流通面积为多个第一流道的流通面积的总和。其中,图7为图5中的C处放大图,在图7中标示201的空白处为一个第一流道201的流通面积。图6为图3中的B-B处的剖面图,以展示在在第一方向X上间隔设置有多个第二流道202,图8为图6中的D处的放大结构图,在图8中标示202的空白处为一个第二流道202的流通面积,而第二流道的总流通面积即图6中多个第二流道的流通面积的总和。图9所示,以一个换热介质通道20为例,一个换热介质通道包括一个第一流道201和两个第二流道202,在第一流道201和第二流道202的在第三方向Z上相同的情况下,两个第二流道202在第一方向X上的宽度大于第一流道201在第一方向上的宽度,因此,两个第二流道的总流通面积大于第一流道的总流通面积。其中,本文中所指的“总流通面积”的计算方法相同。As shown in FIGS. 2 to 3 , the total flow area of the plurality of second flow channels 202 is larger than the total flow area of the first flow channels 201 . When there are multiple first flow channels 201 , the total flow area of the plurality of second flow channels 202 is greater than the total flow area of the plurality of first flow channels 201 . 5 is a cross-sectional view at A-A in FIG. 3 to show that a plurality of first flow channels 201 are arranged at intervals in the first direction X, and the flow areas of the plurality of first flow channels 201 are marked in the figure, where , the total flow area of the first flow channel 201 is the sum of the flow areas of multiple first flow channels. Among them, FIG. 7 is an enlarged view of position C in FIG. 5 , and the blank space marked 201 in FIG. 7 is the flow area of a first flow channel 201 . Figure 6 is a cross-sectional view at B-B in Figure 3 to show that a plurality of second flow channels 202 are spaced in the first direction X. Figure 8 is an enlarged structural view of D in Figure 6. In Figure 8 The blank space marked 202 is the flow area of one second flow channel 202, and the total flow area of the second flow channel is the sum of the flow areas of multiple second flow channels in Figure 6. As shown in Figure 9, taking a heat exchange medium channel 20 as an example, a heat exchange medium channel includes a first flow channel 201 and two second flow channels 202. The third flow channel between the first flow channel 201 and the second flow channel 202 is When the direction Z is the same, the width of the two second flow channels 202 in the first direction X is greater than the width of the first flow channel 201 in the first direction. Therefore, the total flow area of the two second flow channels is larger than the The total flow area of the first channel. Among them, the calculation method of "total circulation area" referred to in this article is the same.
其中,当需要对电池200进行冷却时,换热介质为低温流体,低温流体从换热介质入口11进入,第一流道201与换热介质入口11连通,此时低温流体的温度较低,因此,第一流道201中的冷却效果较好。当低温流体经过第一流道201后,在第一流道201中吸收了部分电池200的热量,进而通过第一流道201后的低温流体的温度相对换热介质入口11处的温度较为上升,导致进入第二流道202的低温流体相对第一流道201的低温流体的吸热能力下降,通过增大第二流道202的总流通面积,使第二流道202的总流通面积大于第一流道201的总流通面积,增大第二流道202的吸热接触面积,提升第二流道202的低温流体的吸热能力,进而解决换热介质通道20在换热介质入口11端与换热介质出口12端的冷却效果差异大的技术问题,使换热板100在第二方向Y上的整体冷却效果均匀,对电池200散热整体更均匀。作为其中一实施例,低温流体为冷却液,如冰水混合物等,当然,换热介质只要能实现对电池实现降温即可。Among them, when the battery 200 needs to be cooled, the heat exchange medium is a low-temperature fluid, and the low-temperature fluid enters from the heat exchange medium inlet 11. The first flow channel 201 is connected with the heat exchange medium inlet 11. At this time, the temperature of the low-temperature fluid is relatively low, so , the cooling effect in the first flow channel 201 is better. When the low-temperature fluid passes through the first flow channel 201 , it absorbs part of the heat of the battery 200 , and then the temperature of the low-temperature fluid after passing through the first flow channel 201 rises relative to the temperature at the heat exchange medium inlet 11 , causing the inlet to The heat absorption capacity of the low-temperature fluid in the second flow channel 202 is reduced relative to the low-temperature fluid in the first flow channel 201. By increasing the total flow area of the second flow channel 202, the total flow area of the second flow channel 202 is larger than that of the first flow channel 201. The total circulation area increases the heat absorption contact area of the second flow channel 202 and improves the heat absorption capacity of the low-temperature fluid in the second flow channel 202, thereby solving the problem of the heat exchange medium channel 20 having a contact with the heat exchange medium at the heat exchange medium inlet 11 end. The technical problem of large difference in cooling effect at the outlet 12 end makes the overall cooling effect of the heat exchange plate 100 in the second direction Y uniform, and the overall heat dissipation of the battery 200 is more uniform. As one embodiment, the low-temperature fluid is a cooling liquid, such as a mixture of ice and water. Of course, the heat exchange medium can be used as long as it can cool down the battery.
当需要对电池200进行加热时,换热介质为高温流体,高温流体从介质入口11进入,第一流道201与换热介质入口11连通,此时,高温流体的温度较高,因此,第一流道201中的高温流体的加热效果较好。当高温流体经过第一流道201后,在第一流道201中向电池200的传递了部分热量,进而通过第一流道201后的高温流体的温度相对换热介质入口11处的温度较为降低,导致进入第二流道202的高温流体相对第一流道201的高温流体的加热能力下降,通过增大第二流道202的总流通面积,使第二流道202的总流通面积大于第一流道201的总流通面积,增大第二流道202的供热面积,提升第二流道202的高温流体的加热能力,进而解决换热介质通道20在换热介质入口11端与换热介质出口12端的加热效果差异大的技术问题,使换热板100在第二方向Y上的整体加热效果均匀,对电池200整体温度差异小。作为其中一实施例,高温流体为温度较高的水,当然,换热介质只要能实现对电池实现加热即可。When the battery 200 needs to be heated, the heat exchange medium is a high-temperature fluid. The high-temperature fluid enters from the medium inlet 11. The first flow channel 201 is connected to the heat exchange medium inlet 11. At this time, the temperature of the high-temperature fluid is relatively high. Therefore, the first flow The high-temperature fluid in Channel 201 has a better heating effect. When the high-temperature fluid passes through the first flow channel 201, part of the heat is transferred to the battery 200 in the first flow channel 201, and the temperature of the high-temperature fluid after passing through the first flow channel 201 is relatively lower than the temperature at the heat exchange medium inlet 11, resulting in The heating capacity of the high-temperature fluid entering the second flow channel 202 is lower than that of the high-temperature fluid in the first flow channel 201. By increasing the total flow area of the second flow channel 202, the total flow area of the second flow channel 202 is larger than that of the first flow channel 201. The total circulation area increases the heating area of the second flow channel 202 and improves the heating capacity of the high-temperature fluid in the second flow channel 202, thus solving the problem between the heat exchange medium inlet 11 end of the heat exchange medium channel 20 and the heat exchange medium outlet 12 The technical problem of large difference in heating effect between the two ends is eliminated, so that the overall heating effect of the heat exchange plate 100 in the second direction Y is uniform, and the overall temperature difference of the battery 200 is small. As one embodiment, the high-temperature fluid is water with a relatively high temperature. Of course, the heat exchange medium only needs to be able to heat the battery.
进一步的,如图2至图3所示,在换热介质通道20中,换热介质在第一流道201内进行热交换后,因此,换热介质进入第二流道202后热交换能力有所下降,换热介质通道20包括一个第一流道201和多个第二流道202,增加第二流道202的数量,使第二流道202的数量比第一流道201的数量多,且相邻的第二流道202沿第一方向X间隔设置,使第二流道202的在换热板100的第一方向X上的位置分布更为均匀。第一流道201与多个第二流道202连通,使第一流道201内的换热介质在第二流道202中实现分流,第一流道201内的换热介质分流至多个第二流道202中,进而使换热介质均匀地分布在多个第二流道202中,保证换热介质在换热板100中的分布均匀性。作为其中一实施例,相邻的换热介质通道20中的第一流道201分别连接不同的第二流道202,或,一个第二流道202分别与相邻的两个第一流道201连通。Further, as shown in Figures 2 to 3, in the heat exchange medium channel 20, after the heat exchange medium performs heat exchange in the first flow channel 201, therefore, after the heat exchange medium enters the second flow channel 202, the heat exchange capacity is The heat exchange medium channel 20 includes a first flow channel 201 and a plurality of second flow channels 202. Increase the number of the second flow channels 202 so that the number of the second flow channels 202 is greater than the number of the first flow channels 201, and Adjacent second flow channels 202 are spaced apart along the first direction X, so that the position distribution of the second flow channels 202 in the first direction X of the heat exchange plate 100 is more uniform. The first flow channel 201 is connected to a plurality of second flow channels 202, so that the heat exchange medium in the first flow channel 201 is divided into the second flow channels 202, and the heat exchange medium in the first flow channel 201 is divided into a plurality of second flow channels. 202, the heat exchange medium is evenly distributed in the plurality of second flow channels 202 to ensure uniform distribution of the heat exchange medium in the heat exchange plate 100. As one embodiment, the first flow channels 201 in adjacent heat exchange medium channels 20 are respectively connected to different second flow channels 202, or one second flow channel 202 is connected to two adjacent first flow channels 201 respectively. .
进一步的,如图4所示,第二流道202沿第二方向Y包括多个子流段2021,子流段2021包括多个子流道2022,在第二方向Y上的相邻两个子流段2021相连通,子流段2021的子流道2022数量沿第二方向Y逐段增加,子流段2021的总流通面积沿第二方向Y逐段增加。第二流道202沿第二方向Y形成多个子流段2021,子流段2021包括多个子流道2022,由于子流道2022的数量沿第二方向Y逐段增加,使子流段越靠近换热介质出口12一端,的子流段2021的子流道2022数量越多,越靠近换热介质出口12一端的子流段2021的子流道2022的总流通面积,以提升靠近换热介质出口12一端的换热介质通道20的散热能力,提升换热介质通道20的整体散热均匀性。Further, as shown in Figure 4, the second flow channel 202 includes a plurality of sub-flow sections 2021 along the second direction Y. The sub-flow sections 2021 include a plurality of sub-flow channels 2022. Two adjacent sub-flow sections in the second direction Y 2021 are connected, the number of sub-flow channels 2022 of the sub-flow section 2021 increases step by step along the second direction Y, and the total flow area of the sub-flow section 2021 increases step by step along the second direction Y. The second flow channel 202 forms a plurality of sub-flow sections 2021 along the second direction Y. The sub-flow sections 2021 include a plurality of sub-flow channels 2022. Since the number of the sub-flow channels 2022 increases section by section along the second direction Y, the closer the sub-flow sections are to each other. The greater the number of sub-flow channels 2022 in the sub-flow section 2021 at one end of the heat exchange medium outlet 12, the closer the total flow area of the sub-flow channels 2022 in the sub-flow section 2021 at one end of the heat exchange medium outlet 12 is to increase the total flow area of the sub-flow channels 2022 close to the heat exchange medium outlet 12. The heat dissipation capacity of the heat exchange medium channel 20 at one end of the outlet 12 improves the overall heat dissipation uniformity of the heat exchange medium channel 20 .
作为其中一实施例,在第二方向Y上相邻的两个子流段2021,靠近换热介质出口12的子流段2021为下子流段,靠近换热介质入口11的子流段2021为上子流段,下子流段的子流道2022的数量为上子流段的子流道2022的数量的至少两倍。其中,倍数越大,子流段2021的散热效果更为均匀。As one embodiment, among the two adjacent sub-flow sections 2021 in the second direction Y, the sub-flow section 2021 close to the heat exchange medium outlet 12 is the lower sub-flow section, and the sub-flow section 2021 close to the heat exchange medium inlet 11 is the upper sub-flow section. In the sub-flow section, the number of sub-flow channels 2022 in the lower sub-flow section is at least twice the number of sub-flow channels 2022 in the upper sub-flow section. Among them, the larger the multiple, the more uniform the heat dissipation effect of the sub-flow section 2021.
进一步的,如图4所示,子流段2021中的其中一个子流道2022与靠近换热介质出口12的相邻的子流段2021中的多个子流道2022连通,以使子流道2022在第二方向Y上朝向换热介质出口12一端实现逐渐分流,在第二方向Y上朝向换热介质出口12一端的子流道2022数量逐渐变多,通过增加子流道2022数量提升朝向换热介质出口12一端的散热能力,提升第二流道202的整体散热均匀性。Further, as shown in Figure 4, one of the sub-flow channels 2022 in the sub-flow section 2021 is connected with multiple sub-flow channels 2022 in the adjacent sub-flow section 2021 close to the heat exchange medium outlet 12, so that the sub-flow channels 2022 gradually divides the flow toward the heat exchange medium outlet 12 in the second direction Y. The number of sub-flow channels 2022 toward the heat exchange medium outlet 12 in the second direction Y gradually increases. By increasing the number of sub-flow channels 2022, the direction is improved. The heat dissipation capability of one end of the heat exchange medium outlet 12 improves the overall heat dissipation uniformity of the second flow channel 202 .
进一步的,如图2至图4所示,子流段2021的子流道2022的宽度沿第二方向Y逐段减小,子流段2021的子流道2022在第一方向X之间的间距沿第二方向Y逐段减小。在换热板100在第一方向X上宽度保持一定的情况下,由于子流段2021在第二方向Y上朝向换热介质出口12一端的子流道2022的数量逐渐增加,子流道2022在第一方向X上的宽度以及在第一方向X上相邻的子流道2022之间的间距逐渐减小,通过设置子流道2022的宽度以及相邻子流道2022之间的间距以提升第二流道202在第二方向Y上的散热均匀性。Further, as shown in Figures 2 to 4, the width of the sub-flow channel 2022 of the sub-flow section 2021 is gradually reduced along the second direction Y, and the width of the sub-flow channel 2022 of the sub-flow section 2021 is between the first direction The spacing decreases step by step along the second direction Y. When the width of the heat exchange plate 100 remains constant in the first direction The width in the first direction X and the spacing between adjacent sub-flow channels 2022 in the first direction The heat dissipation uniformity of the second flow channel 202 in the second direction Y is improved.
进一步的,如图2至图3所示,相邻的两个第二流道202在第一方向X之间的间距小于相邻的第一流道201在第一方向X之间的间距。由于第二流道202的总流通面积大于第一流道201的总流通面积,同时,第二流道202在第一方向X之间的间距小于相邻的第一流道201之间的间距,提升第二流道202在第一方向X上的散热均匀性。Further, as shown in FIGS. 2 to 3 , the distance between two adjacent second flow channels 202 in the first direction X is smaller than the distance between adjacent first flow channels 201 in the first direction X. Since the total flow area of the second flow channel 202 is larger than the total flow area of the first flow channel 201, and at the same time, the distance between the second flow channels 202 in the first direction X is smaller than the distance between the adjacent first flow channels 201, the improvement The heat dissipation uniformity of the second flow channel 202 in the first direction X.
作为其中一实施例,如图2至图3所示,相邻的第一流道201在第一方向X上的间隔设置在5-100mm,相邻的第二流道202在第一方向X上的间隔设置在1-50mm,第二流道202在第一方向X上的布置数量大于第一流道201的布置数量,同时,第二流道202在第一方向X上的间隔小于第一流道201的间隔,使第二流道202在第一方向X上的布置密度大于第一流道201的布置密度,提升第二流道202的冷却效果更为均匀。当然,相邻的子流道2022在第一方向X的间隔设置在1-50mm,子流道2022在第一方向X的间距沿第二方向Y朝向换热介质出口12一端逐渐变小,使靠近换热介质出口12一端的子流道2022之间的间距逐渐缩小,子流道2022的密度增大,提升换热介质出口12一端的冷却支流的冷却效果,进而提升换热板100从换热介质入口11至换热介质出口12之间的冷却效果的均匀性。As one embodiment, as shown in FIGS. 2 to 3 , the spacing between adjacent first flow channels 201 in the first direction X is set at 5-100 mm, and the spacing between adjacent second flow channels 202 in the first direction The spacing is set at 1-50 mm. The number of second flow channels 202 arranged in the first direction X is greater than the number of first flow channels 201. At the same time, the spacing of the second flow channels 202 in the first direction The spacing of 201 makes the arrangement density of the second flow channels 202 in the first direction X greater than that of the first flow channels 201, thereby improving the cooling effect of the second flow channels 202 to be more uniform. Of course, the spacing between adjacent sub-flow channels 2022 in the first direction X is set at 1-50 mm, and the spacing between the sub-flow channels 2022 in the first direction The distance between the sub-flow channels 2022 near the end of the heat exchange medium outlet 12 gradually decreases, and the density of the sub-flow channels 2022 increases, which improves the cooling effect of the cooling branch flow at one end of the heat exchange medium outlet 12, thereby improving the efficiency of the heat exchange plate 100. The uniformity of the cooling effect between the heat medium inlet 11 and the heat exchange medium outlet 12.
进一步的,如图7所示,换热介质通道20在第三方向Z上的高度h占换热板100的总厚度H的50%-75%,在保持换热板100总体支撑强度的基础上,使换热介质通道20在第三方向Z上设置较大的高度,增加换热介质通道20内冷却液的容量,提升换热介质通道20的散热效果。其中,第一方向X、第二方向Y以及第三方向Z相互相交。Further, as shown in Figure 7, the height h of the heat exchange medium channel 20 in the third direction Z accounts for 50%-75% of the total thickness H of the heat exchange plate 100, on the basis of maintaining the overall support strength of the heat exchange plate 100. , the heat exchange medium channel 20 is set to a larger height in the third direction Z, thereby increasing the capacity of the cooling liquid in the heat exchange medium channel 20 and improving the heat dissipation effect of the heat exchange medium channel 20 . Among them, the first direction X, the second direction Y and the third direction Z intersect with each other.
进一步的,如图2至图3所示,换热板100沿第二方向Y的相对两端分别设有沿第一方向X延伸的换热介质流入槽21和换热介质流出槽22,多个换热介质通道20的第一流道201通过换热介质流入槽21与换热介质入口11连通,多个换热介质通道20的第二流道202通过换热介质流出槽22与换热介质出口12连通。换热介质流入槽21位于换热介质入口11与第一流道201之间,通过换热介质流入槽21为冷却液从换热介质入口11进入后提供一个缓存空间,使冷却液进入第一流道201的流速更为稳定,同时,多个第一流道201分别与换热介质流入槽21连通,使换热介质流入槽21中的冷却液分流至多个第一流道201,使冷却液的分流更为均匀。换热介质流出槽22位于换热介质出口12与第二流道202之间,多个第二流道202均与换热介质流出槽22连通,冷却液从第二流道202进入换热介质流出槽22,换热介质流出槽22为多个第二流道202提供了汇集空间,使冷却液进入换热介质出口12的流速更为稳定。通过换热介质流入槽21和换热介质流出槽22的设置,使换热介质通道20内的冷却液流动更为顺畅更为稳定。其中,换热介质流入槽21和换热介质流出槽22的形状不做限定,作为其中一实施例,换热介质流出槽22和换热介质流入槽21均为沿第一方向X延伸的长方形,更便于加工,同时能满足沿第一方向X间隔设置第一流道201和第二流道202的连接,满足第一流道201和第二流道202在第一方向X上散热均匀性的需求。Further, as shown in Figures 2 to 3, the opposite ends of the heat exchange plate 100 along the second direction Y are respectively provided with a heat exchange medium inflow groove 21 and a heat exchange medium outflow groove 22 extending along the first direction X. The first flow channel 201 of each heat exchange medium channel 20 is connected to the heat exchange medium inlet 11 through the heat exchange medium inlet groove 21, and the second flow channels 202 of the plurality of heat exchange medium channels 20 are connected to the heat exchange medium through the heat exchange medium outflow groove 22. Exit 12 is connected. The heat exchange medium inflow groove 21 is located between the heat exchange medium inlet 11 and the first flow channel 201. The heat exchange medium inflow groove 21 provides a buffer space for the cooling liquid after entering from the heat exchange medium inlet 11, so that the cooling liquid enters the first flow channel. 201, the flow rate is more stable. At the same time, the plurality of first flow channels 201 are respectively connected with the heat exchange medium inflow groove 21, so that the cooling liquid in the heat exchange medium inflow groove 21 is diverted to the plurality of first flow passages 201, so that the cooling liquid is more divided. for uniformity. The heat exchange medium outflow groove 22 is located between the heat exchange medium outlet 12 and the second flow channel 202. The plurality of second flow channels 202 are all connected with the heat exchange medium outflow groove 22. The cooling liquid enters the heat exchange medium from the second flow channel 202. The outflow groove 22 and the heat exchange medium outflow groove 22 provide a collection space for the plurality of second flow channels 202, so that the flow rate of the cooling liquid into the heat exchange medium outlet 12 is more stable. Through the arrangement of the heat exchange medium inflow groove 21 and the heat exchange medium outflow groove 22, the cooling liquid flow in the heat exchange medium channel 20 is made smoother and more stable. The shapes of the heat exchange medium inflow groove 21 and the heat exchange medium outflow groove 22 are not limited. As one embodiment, the heat exchange medium outflow groove 22 and the heat exchange medium inflow groove 21 are both rectangular shapes extending along the first direction X. , is more convenient for processing, and at the same time can meet the connection of the first flow channel 201 and the second flow channel 202 arranged at intervals along the first direction .
作为其中一实施例,如图2至图3所示,换热介质流入槽21和换热介质流出槽22在第二方向Y上的宽度大于或等于0.1mm,换热介质流入槽21和换热介质流出槽22设置在一定宽度,为冷却液提供适度的缓存空间。换热介质流入槽21和换热介质流出槽22的深度分别与换热介质通道20在第三方向Z上的厚度保持一致,使换热介质的流动更为顺畅。As one of the embodiments, as shown in FIGS. 2 to 3 , the widths of the heat exchange medium inflow groove 21 and the heat exchange medium outflow groove 22 in the second direction Y are greater than or equal to 0.1 mm. The heat medium outflow groove 22 is set at a certain width to provide a moderate buffer space for the cooling liquid. The depths of the heat exchange medium inflow groove 21 and the heat exchange medium outflow groove 22 are respectively consistent with the thickness of the heat exchange medium channel 20 in the third direction Z, making the flow of the heat exchange medium smoother.
进一步的,如图2和图5至图7所示,换热板100包括盖板1和基板2,盖板1与基板2密封连接形成换热板100,避免换热介质的渗漏。需要说明的是,盖板1和基板2的连接方式包括但不仅限于激光焊接、超声波焊接、胶粘剂胶接或热压、纳米注塑。换热板100分为盖板1和基板2,换热板100为分体式结构,更便于换热介质通道20的加工。其中,盖板1中的换热介质通道20,换热介质通道20为槽结构,换热介质通道20的开口朝向基板2,通过基板2将换热介质通道20的槽口密封形成流道结构。或,基板2设有换热介质通道20,基板2中的换热介质通道20,换热介质通道20为槽结构,换热介质通道20的开口朝向盖板1,通过盖板1将换热介质通道20的槽口密封形成流道结构。在盖板1或基板2上设置换热介质通道20,加工方法简单,组装方法简单,均能实现换热介质通道20在换热板100中的设置。Further, as shown in Figure 2 and Figures 5 to 7, the heat exchange plate 100 includes a cover plate 1 and a base plate 2. The cover plate 1 and the base plate 2 are sealingly connected to form the heat exchange plate 100 to avoid leakage of the heat exchange medium. It should be noted that the connection method between the cover plate 1 and the base plate 2 includes but is not limited to laser welding, ultrasonic welding, adhesive bonding or hot pressing, and nano-injection molding. The heat exchange plate 100 is divided into a cover plate 1 and a base plate 2. The heat exchange plate 100 has a split structure, which is more convenient for processing the heat exchange medium channel 20. Among them, the heat exchange medium channel 20 in the cover plate 1 has a groove structure. The opening of the heat exchange medium channel 20 faces the base plate 2. The slot of the heat exchange medium channel 20 is sealed by the base plate 2 to form a flow channel structure. . Or, the base plate 2 is provided with a heat exchange medium channel 20. The heat exchange medium channel 20 in the base plate 2 has a groove structure. The opening of the heat exchange medium channel 20 faces the cover plate 1, and the heat exchange medium channel 20 is passed through the cover plate 1. The slot seal of the medium channel 20 forms a flow channel structure. The heat exchange medium channel 20 is provided on the cover plate 1 or the base plate 2. The processing method is simple and the assembly method is simple, and the heat exchange medium channel 20 can be installed in the heat exchange plate 100.
基板2与盖板1的相对面分别设有换热介质通道20。基板2上设置换热介质通道20,盖板1也设置有换热介质通道20,基板2上的换热介质通道20和盖板1上的换热介质通道20可以是分别两个独立的换热介质通道20。由于盖板1和基板2均设置有换热介质通道20,换热介质通道20数量增加,换热板100内换热介质的容量更大,冷却效果更佳。基板2和盖板1上的换热介质通道20均为槽结构且槽口相对设置,盖板1和基板2上换热介质通道20的位置和结构均对应设置,以使基板2和盖板1上的换热介质通道20通过槽口连通,有助于提升换热介质通道20在第三方向Z上的深度,即换热板100内换热介质的容量更大,热交换效果更佳。Heat exchange medium channels 20 are respectively provided on the opposite surfaces of the base plate 2 and the cover plate 1 . The base plate 2 is provided with a heat exchange medium channel 20, and the cover plate 1 is also provided with a heat exchange medium channel 20. The heat exchange medium channel 20 on the base plate 2 and the heat exchange medium channel 20 on the cover plate 1 can be two independent exchangers. Thermal medium channel 20. Since both the cover plate 1 and the base plate 2 are provided with heat exchange medium channels 20, the number of heat exchange medium channels 20 is increased, the capacity of the heat exchange medium in the heat exchange plate 100 is larger, and the cooling effect is better. The heat exchange medium channels 20 on the base plate 2 and the cover plate 1 are both groove structures and the slots are arranged oppositely. The positions and structures of the heat exchange medium channels 20 on the cover plate 1 and the base plate 2 are set correspondingly, so that the base plate 2 and the cover plate The heat exchange medium channel 20 on 1 is connected through the slot, which helps to increase the depth of the heat exchange medium channel 20 in the third direction Z, that is, the heat exchange medium capacity in the heat exchange plate 100 is larger and the heat exchange effect is better. .
作为其中一实施例,如图5所示,盖板1通过冲压、挤压或铸造制成,盖板1厚度设置在0.1-5mm,盖板1的材质为金属材料,如铜合金、铝合金或镁合金等。由于金属材料导热性较好,基板2设置有槽结构的换热介质通道20,换热介质通道20的槽口朝向盖板1,通过盖板1对换热介质通道20的槽口进行密封,至少盖板1与电池200抵贴接触,加快换热板100内的换热介质与电池进行热交换,提升电池200与换热板100的换热介质之间的热传导效率。As one embodiment, as shown in Figure 5, the cover plate 1 is made by stamping, extrusion or casting. The thickness of the cover plate 1 is set at 0.1-5mm. The cover plate 1 is made of metal materials, such as copper alloy and aluminum alloy. Or magnesium alloy, etc. Since metal materials have good thermal conductivity, the base plate 2 is provided with a heat exchange medium channel 20 with a groove structure. The notch of the heat exchange medium channel 20 faces the cover plate 1, and the notch of the heat exchange medium channel 20 is sealed by the cover plate 1. At least the cover plate 1 is in close contact with the battery 200, which accelerates the heat exchange between the heat exchange medium in the heat exchange plate 100 and the battery, and improves the heat conduction efficiency between the battery 200 and the heat exchange medium of the heat exchange plate 100.
作为其中一实施例,如图1所示,盖板1或基板2通过粘胶方式固定于电池200热量较高的位置,粘胶为导热结构胶或导热结构胶带。As one of the embodiments, as shown in FIG. 1 , the cover 1 or the substrate 2 is fixed on the high-heat position of the battery 200 through adhesive. The adhesive is a thermally conductive structural glue or a thermally conductive structural tape.
作为其中一实施例,如图2至图3所示,基板2通过注塑形成,厚度设置在0.1mm-20mm,基板2的材料为塑胶,如尼龙、聚苯硫醚、聚对苯二甲酸丁二酯、聚丙烯等,基板2为塑胶时,利用塑胶材料的低导热性对动力电池200进行低温保温。As one embodiment, as shown in Figures 2 to 3, the substrate 2 is formed by injection molding, with a thickness set at 0.1mm-20mm. The material of the substrate 2 is plastic, such as nylon, polyphenylene sulfide, polybutylene terephthalate. Diester, polypropylene, etc., when the substrate 2 is made of plastic, the low thermal conductivity of the plastic material is used to insulate the power battery 200 at low temperature.
进一步的,如图2和图6所示,换热板100还包括第一接头3和第二接头4,换热板100设有换热介质入口11和换热介质出口12,第一接头3通过换热介质入口11与第一流道201连通,第二接头4通过换热介质出口12与第二流道202连通。换热介质从第一接头3进入第一流道201,从第二流道202通过第二接头4排出,通过第一接头3和第二接头4的设置,更便于换热介质的接入和排出。作为其中一实施例,第一接头3和第二接头4均设置于盖板1或基板2,或第一接头3设置在盖板1,第二接头4设置在基板2,或第一接头3设置在基板2,第二接头4设置在盖板1,只要第一接头3能与换热介质入口11连通,第二接头4能与换热介质出口12连通即可。当然,作为其中一实施例,第一接头3通过换热介质入口11与换热介质流入槽21连通,第二接头4通过换热介质出口12与换热介质流出槽22连通。Further, as shown in Figures 2 and 6, the heat exchange plate 100 also includes a first joint 3 and a second joint 4. The heat exchange plate 100 is provided with a heat exchange medium inlet 11 and a heat exchange medium outlet 12. The first joint 3 The heat exchange medium inlet 11 communicates with the first flow channel 201 , and the second joint 4 communicates with the second flow channel 202 through the heat exchange medium outlet 12 . The heat exchange medium enters the first flow channel 201 from the first joint 3 and is discharged from the second flow channel 202 through the second joint 4. The arrangement of the first joint 3 and the second joint 4 makes it easier to access and discharge the heat exchange medium. . As one embodiment, both the first connector 3 and the second connector 4 are provided on the cover plate 1 or the base plate 2, or the first connector 3 is provided on the cover plate 1, and the second connector 4 is provided on the base plate 2, or the first connector 3 It is provided on the base plate 2 and the second joint 4 is provided on the cover plate 1 , as long as the first joint 3 can communicate with the heat exchange medium inlet 11 and the second joint 4 can communicate with the heat exchange medium outlet 12 . Of course, as one embodiment, the first joint 3 is connected to the heat exchange medium inflow groove 21 through the heat exchange medium inlet 11 , and the second joint 4 is connected to the heat exchange medium outflow groove 22 through the heat exchange medium outlet 12 .
进一步的,电池包还包括:箱体,箱体具有容纳腔,电池200和换热板100均设于容纳腔内;通过容纳腔实现对电池200和换热板100的固定和限位,使换热板100的至少一侧与电池200抵贴,保证换热板100对电池200的热交换效果。或框体,框体和换热板100共同限定出容纳腔,电池200设于容纳腔内。通过容纳腔实现对电池200的固定和限位,防止电池200远离换热板100,保证换热板100对电池200的热交换效果。其中,通过框体对电池200进行固定,实现轻量化设置。Further, the battery pack also includes: a box body with a receiving cavity, in which the battery 200 and the heat exchange plate 100 are disposed; the battery 200 and the heat exchange plate 100 are fixed and limited through the receiving cavity, so that the battery 200 and the heat exchange plate 100 are fixed and limited. At least one side of the heat exchange plate 100 is in contact with the battery 200 to ensure the heat exchange effect of the heat exchange plate 100 on the battery 200 . Or a frame, the frame and the heat exchange plate 100 jointly define a receiving cavity, and the battery 200 is disposed in the receiving cavity. The battery 200 is fixed and limited through the accommodation cavity, preventing the battery 200 from moving away from the heat exchange plate 100 and ensuring the heat exchange effect of the heat exchange plate 100 on the battery 200. Among them, the battery 200 is fixed through the frame to achieve lightweight installation.
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型技术原理的前提下,还可以做出若干改进和替换,这些改进和替换也应视为本实用新型的保护范围。The above are only preferred embodiments of the present invention. It should be pointed out that those skilled in the art can make several improvements and substitutions without departing from the technical principles of the present invention. These improvements and replacement should also be regarded as the protection scope of the present utility model.
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