CN111900143A - A manifold type high aspect ratio microchannel heat exchanger - Google Patents
A manifold type high aspect ratio microchannel heat exchanger Download PDFInfo
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- CN111900143A CN111900143A CN202010760271.2A CN202010760271A CN111900143A CN 111900143 A CN111900143 A CN 111900143A CN 202010760271 A CN202010760271 A CN 202010760271A CN 111900143 A CN111900143 A CN 111900143A
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- 239000000110 cooling liquid Substances 0.000 claims abstract description 18
- 239000007788 liquid Substances 0.000 claims description 84
- 239000002826 coolant Substances 0.000 claims description 42
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 239000010949 copper Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 239000011550 stock solution Substances 0.000 claims 5
- 238000010521 absorption reaction Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 9
- 230000006911 nucleation Effects 0.000 abstract description 5
- 238000010899 nucleation Methods 0.000 abstract description 5
- 238000001816 cooling Methods 0.000 abstract description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000010892 electric spark Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000011900 installation process Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000004377 microelectronic Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L23/00—Details of semiconductor or other solid state devices
- H01L23/34—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements
- H01L23/46—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements involving the transfer of heat by flowing fluids
- H01L23/473—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements involving the transfer of heat by flowing fluids by flowing liquids
- H01L23/4735—Jet impingement
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L23/00—Details of semiconductor or other solid state devices
- H01L23/34—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements
- H01L23/36—Selection of materials, or shaping, to facilitate cooling or heating, e.g. heatsinks
- H01L23/367—Cooling facilitated by shape of device
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Abstract
本发明公开了一种歧管式高深宽比微通道换热器,包括上盖板、歧管装置及微通道热沉,上盖板盖合于微通道热沉的上方,上盖板的第一表面上开设有一内腔体,歧管装置设置于内腔体的顶壁上,微通道热沉的第一表面上设有与歧管装置的位置相对应的微肋壁,歧管装置与微肋壁上下贴合容纳于内腔体内,微肋壁沿冷却液流动方向形成若干平行排布的高深宽比槽道,歧管装置与若干槽道构成歧式射流微通道腔体,歧管装置可加强微通道内流动的扰动,强化换热,实现射流冷却方式,且使热沉底部温度分布更加均匀,高深宽比槽道与歧管装置紧密相连,可提高换热面积,提供大量气泡成核点,进一步提高换热效果,且有效降低压降。
The invention discloses a manifold type high aspect ratio micro-channel heat exchanger, comprising an upper cover plate, a manifold device and a micro-channel heat sink, the upper cover plate is covered above the micro-channel heat sink, and the first There is an inner cavity on one surface, the manifold device is arranged on the top wall of the inner cavity, the first surface of the microchannel heat sink is provided with a micro-rib wall corresponding to the position of the manifold device, and the manifold device is connected with The micro-rib wall is attached up and down and accommodated in the inner cavity. The micro-rib wall forms several parallel channels with high aspect ratio along the flow direction of the cooling liquid. The manifold device and several channels form a manifold jet micro-channel cavity. The manifold The device can strengthen the disturbance of the flow in the microchannel, strengthen the heat exchange, realize the jet cooling method, and make the temperature distribution at the bottom of the heat sink more uniform. The high aspect ratio channel is closely connected with the manifold device, which can increase the heat exchange area and provide a large number of bubbles The nucleation point further improves the heat transfer effect and effectively reduces the pressure drop.
Description
技术领域technical field
本发明属于微通道换热器设计领域,尤其涉及一种歧管式高深宽比微通道换热器。The invention belongs to the field of microchannel heat exchanger design, in particular to a manifold type high aspect ratio microchannel heat exchanger.
背景技术Background technique
电子设备的高速集成化和微型化,使得散热问题尤为显著,早在1981年,有学者提出利用微通道进行换热,不仅能够满足高热流密度的需求,而且有效解决了常规通道尺寸不适用于微电子设备的问题。随着对微通道换热器研究的深入,不同结构的微通道,对换热效果有不同的影响。相较于单相流动,微通道内沸腾流动换热具有更高效的换热能力,其充分利用冷却剂的相变潜热,沸腾过程中气泡的生长、脱离、破碎等过程大大提高换热系数,以满足更高换热需求的电子设备。The high-speed integration and miniaturization of electronic equipment make the heat dissipation problem particularly significant. As early as 1981, some scholars proposed to use microchannels for heat exchange, which not only can meet the needs of high heat flux density, but also effectively solve the problem that the size of conventional channels is not suitable for Problems with Microelectronics. With the deepening of research on microchannel heat exchangers, microchannels with different structures have different effects on the heat transfer effect. Compared with single-phase flow, the boiling flow heat transfer in the microchannel has a more efficient heat transfer capacity. It makes full use of the latent heat of the phase change of the coolant, and the growth, detachment, and fragmentation of bubbles during the boiling process greatly improves the heat transfer coefficient. Electronic equipment to meet higher heat transfer requirements.
目前微通道换热器大多采用低深宽比微通道换热器,其虽然能够提升换热效果,但换热面积较小,为气泡成核提供的空间不足,导致其换热能力有限,且较小的流道截面使得冷却剂流经微通道时压降较大,导致其功耗增加。专利CN201921304518.9公开了与铝基板复合的高深宽比泡沫金属微通道相变冷却装置,其采用高深宽比微通道,增大换热面积,增加汽化核心密度,有效提高换热系数,但是仅深宽比为5~10,对换热效果的提升有限。At present, most microchannel heat exchangers use low aspect ratio microchannel heat exchangers. Although they can improve the heat exchange effect, the heat exchange area is small, and the space provided for bubble nucleation is insufficient, resulting in limited heat exchange capacity. The smaller cross section of the flow channel causes a larger pressure drop when the coolant flows through the microchannel, resulting in an increase in its power consumption. Patent CN201921304518.9 discloses a high aspect ratio foam metal microchannel phase change cooling device compounded with an aluminum substrate, which adopts high aspect ratio microchannels to increase the heat exchange area, increase the vaporization core density, and effectively improve the heat transfer coefficient, but only The aspect ratio is 5 to 10, and the improvement of heat transfer effect is limited.
大量研究发现,微通道换热器还存在一些问题,诸如并行微通道流量分配不均匀导致微通道底部温度分布不均匀,容易使局部温度升高,进而对电子设备产生不利的影响。专利CN201811088661.9公开了一种多歧式射流微通道芯片液冷散热装置,通过射流作用,一方面加强扰动,提高换热能力,另一方面通过歧管结构有助于流量合理分配,提高热沉底部温度均匀性。但是此微通道换热器需要五个结构模块叠加起来,对加工精度要求较高,且对齐安装过程中容易出现偏差,使流动受阻。A large number of studies have found that there are still some problems in microchannel heat exchangers, such as uneven flow distribution of parallel microchannels, which leads to uneven temperature distribution at the bottom of microchannels, which is easy to increase local temperature, which in turn has adverse effects on electronic equipment. Patent CN201811088661.9 discloses a liquid-cooled heat dissipation device for a multi-manifold jet microchannel chip. Through the action of jets, on the one hand, the disturbance is enhanced and the heat exchange capacity is improved; Temperature uniformity at the bottom of the sink. However, this microchannel heat exchanger requires five structural modules to be superimposed, which requires high machining accuracy, and is prone to deviation during the alignment and installation process, which hinders the flow.
发明内容SUMMARY OF THE INVENTION
本发明的目的是提供一种歧管式高深宽比微通道换热器,可加强微通道内流动扰动,实现射流冷却方式从而强化换热,且使热沉底部温度分布更为均匀;高深宽比微通道提高换热面积,提供大量气泡成核点,进一步提高换热效果,且有效降低压降。The purpose of the present invention is to provide a manifold type high aspect ratio microchannel heat exchanger, which can strengthen the flow disturbance in the microchannel, realize the jet cooling method to strengthen the heat exchange, and make the temperature distribution at the bottom of the heat sink more uniform; Compared with microchannels, the heat exchange area is increased, a large number of bubble nucleation points are provided, the heat exchange effect is further improved, and the pressure drop is effectively reduced.
为解决上述问题,本发明的技术方案为:For solving the above problems, the technical scheme of the present invention is:
一种歧管式高深宽比微通道换热器,包括上盖板、歧管装置及微通道热沉,所述上盖板盖合于所述微通道热沉的上方,将所述上盖板与所述微通道热沉贴合的面分别定义为所述上盖板的第一表面和所述微通道热沉的第一表面;A manifold type high aspect ratio microchannel heat exchanger, comprising an upper cover plate, a manifold device and a microchannel heat sink, the upper cover plate is covered above the microchannel heat sink, and the upper cover The surfaces on which the plate is attached to the microchannel heat sink are respectively defined as the first surface of the upper cover plate and the first surface of the microchannel heat sink;
所述上盖板上开设有冷却剂入口和冷却剂出口,所述上盖板的第一表面上开设有一内腔体;The upper cover plate is provided with a coolant inlet and a coolant outlet, and an inner cavity is defined on the first surface of the upper cover plate;
所述歧管装置设置于所述内腔体的顶壁上,所述歧管装置包括至少一个进液流道和至少一个出液流道;The manifold device is arranged on the top wall of the inner cavity, and the manifold device includes at least one liquid inlet flow channel and at least one liquid outlet flow channel;
所述微通道热沉的第一表面上设有与所述歧管装置的位置相对应的微肋壁,当所述上盖板与所述微通道热沉处于盖合状态时,所述歧管装置与所述微肋壁上下贴合容纳于所述内腔体内,并将所述内腔体分隔成独立的入口储液腔和出口储液腔,所述微肋壁沿冷却液流动方向形成若干平行排布的高深宽比槽道,所述歧管装置与若干所述槽道构成歧式射流微通道腔体,所述进液流道与若干所述槽道一一导通,所述出液流道与若干所述槽道一一导通;The first surface of the micro-channel heat sink is provided with a micro-rib wall corresponding to the position of the manifold device. When the upper cover plate and the micro-channel heat sink are in a covered state, the manifold The tube device and the micro-rib wall are attached up and down to be accommodated in the inner cavity, and the inner cavity is divided into independent inlet liquid storage chambers and outlet liquid storage chambers, and the micro-rib walls are along the flow direction of the cooling liquid A plurality of high aspect ratio channels arranged in parallel are formed, the manifold device and a plurality of the channels constitute a manifold jet micro-channel cavity, and the liquid inlet channel is connected to the plurality of the channels one by one, so the The said liquid flow channel is connected with a plurality of said channels one by one;
所述冷却剂入口与所述入口储液腔的进液口连通,所述入口储液腔的出液口与所述进液流道连通,冷却液经由所述进液流道射流进入所述槽道内,所述出液流道与所述出口储液腔的进液口连通,所述出口储液腔的出液口与所述冷却剂出口连通,吸收热量的冷却液从所述槽道依次经所述出液流道、所述出口储液腔从所述冷却剂出口导出。The coolant inlet is communicated with the liquid inlet of the inlet liquid storage cavity, the liquid outlet of the inlet liquid storage cavity is communicated with the liquid inlet channel, and the cooling liquid enters the In the channel, the liquid outlet channel is communicated with the liquid inlet of the outlet liquid storage cavity, the liquid outlet of the outlet liquid storage cavity is communicated with the coolant outlet, and the cooling liquid that absorbs heat flows from the channel It is led out from the coolant outlet through the liquid outlet channel and the outlet liquid storage chamber in sequence.
优选地,所述歧管装置为设置于所述内腔体的顶壁上的曲形凸肋,所述曲形凸肋的两端延伸至与所述内腔体的侧壁相连,所述曲形凸肋开口朝向所述入口储液腔的弯道为所述进液流道,所述曲形凸肋开口朝向所述出口储液腔的弯道为所述出液流道。Preferably, the manifold device is a curved rib disposed on the top wall of the inner cavity, two ends of the curved rib extend to connect with the side wall of the inner cavity, the The curved rib opening toward the inlet liquid storage chamber is the liquid inlet channel, and the curved rib opening facing the outlet liquid storage chamber is the liquid outlet channel.
优选地,所述歧管装置为W形曲形凸肋,所述W形曲形凸肋与所述内腔体的侧壁构成交替排列的两个进液流道和三个出液流道。Preferably, the manifold device is a W-shaped curved rib, and the W-shaped curved rib and the side wall of the inner cavity form two liquid inlet flow channels and three liquid outlet flow channels arranged alternately. .
优选地,所述进液流道为沿冷却液流动方向渐缩的梯形形状,靠近所述内腔体的侧壁的所述出液流道为沿冷却液流动方向渐扩的直角三角形形状,远离所述内腔体的侧壁的所述出液流道为沿冷却液流动方向渐扩的梯形形状。Preferably, the liquid inlet channel is in the shape of a trapezoid tapering along the flow direction of the cooling liquid, and the liquid outlet channel near the side wall of the inner cavity is in the shape of a right-angled triangle that gradually expands along the flow direction of the cooling liquid, The liquid outlet channel away from the side wall of the inner cavity is in the shape of a trapezoid that gradually expands along the cooling liquid flow direction.
优选地,所述歧管装置采用电火花技术与所述上盖板一体成型加工。Preferably, the manifold device is integrally formed with the upper cover plate by means of electric spark technology.
优选地,所述槽道的深宽比为25。Preferably, the aspect ratio of the channel is 25.
优选地,所述槽道的截面为矩形。Preferably, the cross section of the channel is rectangular.
优选地,所述上盖板、所述歧管装置及所述微通道热沉的材质均为铜。Preferably, the materials of the upper cover plate, the manifold device and the microchannel heat sink are all copper.
优选地,所述微通道热沉的第一表面上开设有与所述内腔体相对应的密封槽。Preferably, a sealing groove corresponding to the inner cavity is formed on the first surface of the microchannel heat sink.
本发明由于采用以上技术方案,使其与现有技术相比具有以下的优点和积极效果:Compared with the prior art, the present invention has the following advantages and positive effects due to the adoption of the above technical solutions:
1)本发明提供了一种歧管式高深宽比微通道换热器,包括上盖板、歧管装置及微通道热沉,上盖板盖合于微通道热沉的上方,上盖板上开设有冷却剂入口和冷却剂出口,上盖板的第一表面上开设有一内腔体,歧管装置设置于内腔体的顶壁上,微通道热沉的第一表面上设有与歧管装置的位置相对应的微肋壁,歧管装置与微肋壁上下堆叠容纳于内腔体内,微肋壁沿冷却液流动方向形成若干平行排布的高深宽比槽道,歧管装置与若干槽道构成歧式射流微通道腔体,歧管装置可加强微通道内流动的扰动,强化换热,实现射流冷却方式,且使热沉底部温度分布更加均匀,高深宽比槽道与歧管装置紧密相连,可提高换热面积,提供大量气泡成核点,进一步提高换热效果,且有效降低压降。1) The present invention provides a manifold type high aspect ratio microchannel heat exchanger, including an upper cover plate, a manifold device and a microchannel heat sink, the upper cover plate is covered above the microchannel heat sink, and the upper cover plate is A coolant inlet and a coolant outlet are opened on the top, an inner cavity is opened on the first surface of the upper cover plate, the manifold device is arranged on the top wall of the inner cavity, and the first surface of the microchannel heat sink is provided with The position of the manifold device corresponds to the micro-rib wall. The manifold device and the micro-rib wall are stacked up and down and accommodated in the inner cavity. The micro-rib wall forms several parallelly arranged high aspect ratio channels along the cooling liquid flow direction. The manifold device It forms a manifold jet microchannel cavity with several channels. The manifold device can strengthen the disturbance of the flow in the microchannel, strengthen the heat exchange, realize the jet cooling method, and make the temperature distribution at the bottom of the heat sink more uniform. The manifold devices are closely connected, which can increase the heat exchange area, provide a large number of bubble nucleation points, further improve the heat exchange effect, and effectively reduce the pressure drop.
附图说明Description of drawings
图1为本发明实施例提供的一种歧管式高深宽比微通道换热器的结构示意图;1 is a schematic structural diagram of a manifold type high aspect ratio microchannel heat exchanger according to an embodiment of the present invention;
图2为图1中盖板的背面结构示意图;FIG. 2 is a schematic view of the rear structure of the cover plate in FIG. 1;
图3为图1中盖板的背面的俯视图;Fig. 3 is the top view of the back of the cover plate in Fig. 1;
图4为图1中高深宽比微通道热沉的结构示意图;Fig. 4 is the structural schematic diagram of the high aspect ratio microchannel heat sink in Fig. 1;
图5为本发明实施例提供的一种歧管式高深宽比微通道换热器的冷却剂流动原理示意图;5 is a schematic diagram of the coolant flow principle of a manifold type high aspect ratio microchannel heat exchanger according to an embodiment of the present invention;
附图标记说明:Description of reference numbers:
1:上盖板;11:冷却剂入口;12:冷却剂出口;13:内腔体;131:入口储液腔;132:出口储液腔;14:上盖板螺纹孔;2:歧管装置;21:进液流道;22:出液流道;221:主出液流道;222:辅出液流道;3:微通道热沉;31:微肋壁;311:槽道;32:微通道热沉螺纹孔;33:密封槽。1: upper cover plate; 11: coolant inlet; 12: coolant outlet; 13: inner cavity; 131: inlet liquid storage chamber; 132: outlet liquid storage chamber; 14: upper cover plate threaded hole; 2: manifold device; 21: liquid inlet channel; 22: outlet channel; 221: main outlet channel; 222: auxiliary outlet channel; 3: micro-channel heat sink; 31: micro-rib wall; 311: channel; 32: Micro-channel heat sink threaded hole; 33: Seal groove.
具体实施方式Detailed ways
以下结合附图和具体实施例对本发明提出的一种歧管式高深宽比微通道换热器作进一步详细说明。根据下面说明和权利要求书,本发明的优点和特征将更清楚。A manifold type high aspect ratio microchannel heat exchanger proposed by the present invention will be described in further detail below with reference to the accompanying drawings and specific embodiments. The advantages and features of the present invention will become apparent from the following description and claims.
参看图1至图5所示,本发明提供了一种歧管式高深宽比微通道换热器,包括上盖板1、歧管装置2及微通道热沉3,上盖板1盖合于微通道热沉3的上方,将上盖板1与微通道热沉3贴合的面分别定义为上盖板1的第一表面和微通道热沉3的第一表面;1 to 5, the present invention provides a manifold type high aspect ratio microchannel heat exchanger, including an
上盖板1整体尺寸为30mm*25mm,材质为金属铜,上盖板1的左右两侧分别开设有贯通上盖板1的冷却剂入口11和冷却剂出口12,冷却剂入口11距离左侧边缘6.5mm,距离前后边缘均为12.5mm,冷却剂出口12距离右侧边缘6.5mm,距离前后边缘均为12.5mm,冷却剂入口11和冷却剂出口12的直径均为5mm,参看图2所示,上盖板1的第一表面上开设有一内腔体13,内腔体13的深度为7mm,内腔体13包括入口储液腔131和出口储液腔132(说明:图1中标注的131和132指代入口储液腔131和出口储液腔132的底部),冷却剂入口11与入口储液腔131连通,冷却剂出口12与出口储液腔132连通;The overall size of the
在本实施例中,上盖板1上还开设有若干上盖板螺纹孔14,上盖板1与微通道热沉3采用螺纹螺栓进行固定连接,上盖板1的前后两侧边缘各设四个上盖板螺纹孔14,共八个上盖板螺纹孔14,在本实施例中,上盖板螺纹孔14的规格为M2的螺纹孔,参看图2所示,微通道热沉3上与上盖板螺纹孔14相对应的位置上开设八个微通道热沉螺纹孔32,微通道热沉螺纹孔32的规格为M2的螺纹孔,上盖板1与微通道热沉3通过上盖板螺纹孔14与微通道热沉螺纹孔32进行紧固连接。In this embodiment, the
参看图2所示,歧管装置2设置于内腔体13的顶壁上,歧管装置2包括至少一个进液流道和至少一个出液流道,歧管装置2为设置于内腔体13的顶壁上的曲形凸肋,曲形凸肋的两端延伸至与内腔体13的侧壁相连,曲形凸肋开口朝向入口储液腔131的弯道为进液流道,曲形凸肋开口朝向出口储液腔132的弯道为出液流道,参看图3所示,在本实施例中,歧管装置2为W形曲形凸肋,歧管装置2的总尺寸为10mm*10mm,位于内腔体13顶壁的中间位置,曲形凸肋的宽度为1mm,高度为2mm,W形曲形凸肋与内腔体13的侧壁构成交替排列的两个进液流道21和三个出液流道22,其中,进液流道22为沿冷却液流动方向渐缩的梯形形状,进液流道22的靠近入口储液腔131一侧的底边为3mm,另一侧的底板为0.3mm,高度为9mm;出液流道22包括两个主出液流道221和一个辅出液流道222,两个主出液流道221位于内腔体13的侧壁,主出液流道221为沿冷却液流动方向渐扩的直角三角形形状,直角三角形的底边为1.5mm,高度为10mm,辅出液流道222位于两主出液流道221的中间,辅出液流道222为沿冷却液流动方向渐扩的梯形形状,该梯形的上底边为0.3mm,下底边为3mm,高度为9mm;Referring to FIG. 2, the
在本实施例中,歧管装置2采用电火花技术加工于内腔体13的顶壁上,与上盖板1一体成型加工。In the present embodiment, the
微通道热沉3的整体尺寸为30mm*25mm,材质为金属铜,微通道热沉3的第一表面上设有与歧管装置2的位置相对应的微肋壁31,歧管装置2与微肋壁31的长宽尺寸一致,微肋壁31的总尺寸为10mm*10mm*5mm,当上盖板1与微通道热沉3处于盖合状态时,歧管装置2与微肋壁31上下贴合容纳于内腔体13内,中间无缝隙,歧管装置2与微肋壁31上下贴合将内腔体13分隔成独立的入口储液腔131和出口储液腔132,微肋壁31沿冷却液流动方向形成若干平行排布的高深宽比槽道311,在本实施例中,微肋壁31的中间微肋壁高5000μm,宽200μm,长1000μm,微肋壁31的两侧微肋壁高5000μm,宽1100μm,长1000μm,槽道311的截面为矩形,共20条,高5000μm,宽200μm,长1000μm,槽道311的水力直径为385μm,深宽比为25;歧管装置2与若干槽道311构成歧式射流微通道腔体,进液流道21与若干槽道311一一导通,出液流道22与若干槽道311一一导通,在本实施例中,进液流道21采用沿冷却液流动方向渐缩的渐缩歧管,有助于冷却液到达距离入口最远的微通道,出液流道22采用沿冷却液流动方向渐扩的渐扩歧管,有助于流体有效汇集于出口储液腔132内;The overall size of the
冷却剂入口11与入口储液腔131的进液口连通,入口储液腔131的出液口与进液流道21连通,冷却液经由进液流道21射流进入槽道311内,出液流道22与出口储液腔132的进液口连通,出口储液腔132的出液口与冷却剂出口12连通,吸收热量的冷却液从槽道311依次经出液流道22、出口储液腔132从冷却剂出口12导出。The
优选地,微通道热沉3的第一表面上开设有与内腔体13相对应的密封槽33。Preferably, a sealing
参看图5所示,本发明提供的换热器的工作原理为冷却剂的流动方向如图中箭头所示,冷却剂从冷却剂入口11流入入口储液腔131,待入口储液腔131充满冷却剂后,沿水平方向流入进液流道21,进而沿垂直方向流入槽道311内,冷却剂在槽道311中的流动方向为先垂直向下,进而水平流动,最终垂直向上汇集到出液流道22,冷却剂在出液流道22中沿水平方向流动汇集到出口储液腔132,通过冷却剂出口12流出微通道换热器。Referring to FIG. 5 , the working principle of the heat exchanger provided by the present invention is that the flow direction of the coolant is shown by the arrow in the figure, the coolant flows from the
本发明提供了一种歧歧管式高深宽比微通道换热器,包括上盖板1、歧管装置2及微通道热沉3,上盖板1盖合于微通道热沉3的上方,上盖板1上开设有冷却剂入口11和冷却剂出口12,上盖板1的第一表面上开设有一内腔体13,歧管装置2设置于内腔体13的顶壁上,微通道热沉3的第一表面上设有与歧管装置2的位置相对应的微肋壁31,歧管装置2与微肋壁31上下堆叠容纳于内腔体13内,微肋壁31沿冷却液流动方向形成若干平行排布的高深宽比槽道311,歧管装置2与若干槽道311构成歧式射流微通道腔体,歧管装置2可加强微通道内流动的扰动,强化换热,实现射流冷却方式,且使热沉底部温度分布更加均匀,高深宽比槽道与歧管装置紧密相连,可提高换热面积,提供大量气泡成核点,进一步提高换热效果,且有效降低压降。The present invention provides a manifold type high aspect ratio microchannel heat exchanger, comprising an
上面结合附图对本发明的实施方式作了详细说明,但是本发明并不限于上述实施方式。即使对本发明作出各种变化,倘若这些变化属于本发明权利要求及其等同技术的范围之内,则仍落入在本发明的保护范围之中。The embodiments of the present invention have been described in detail above with reference to the accompanying drawings, but the present invention is not limited to the above-mentioned embodiments. Even if various changes are made to the present invention, if these changes fall within the scope of the claims of the present invention and the technical equivalents thereof, they still fall within the protection scope of the present invention.
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