CN115307469B - Multi-source driven high-power loop heat pipe radiating device - Google Patents
Multi-source driven high-power loop heat pipe radiating device Download PDFInfo
- Publication number
- CN115307469B CN115307469B CN202210949782.8A CN202210949782A CN115307469B CN 115307469 B CN115307469 B CN 115307469B CN 202210949782 A CN202210949782 A CN 202210949782A CN 115307469 B CN115307469 B CN 115307469B
- Authority
- CN
- China
- Prior art keywords
- ejector
- steam
- chip
- temperature
- pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 230000017525 heat dissipation Effects 0.000 claims abstract description 27
- 239000007788 liquid Substances 0.000 claims description 58
- 239000012530 fluid Substances 0.000 claims description 22
- 238000002156 mixing Methods 0.000 claims description 18
- 239000002184 metal Substances 0.000 claims description 17
- 229910052751 metal Inorganic materials 0.000 claims description 17
- 239000000843 powder Substances 0.000 claims description 17
- 238000001816 cooling Methods 0.000 claims description 16
- 239000011148 porous material Substances 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 230000007246 mechanism Effects 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000003825 pressing Methods 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000012299 nitrogen atmosphere Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 238000005245 sintering Methods 0.000 claims description 3
- 238000004506 ultrasonic cleaning Methods 0.000 claims description 3
- 238000004321 preservation Methods 0.000 claims description 2
- 230000007723 transport mechanism Effects 0.000 claims description 2
- 238000007789 sealing Methods 0.000 abstract 3
- 238000009835 boiling Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 238000003860 storage Methods 0.000 description 4
- 230000004907 flux Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000005499 meniscus Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 231100000252 nontoxic Toxicity 0.000 description 3
- 230000003000 nontoxic effect Effects 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 150000003839 salts Chemical group 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 230000005514 two-phase flow Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/04—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with tubes having a capillary structure
- F28D15/043—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with tubes having a capillary structure forming loops, e.g. capillary pumped loops
-
- 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
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/06—Control arrangements therefor
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K7/00—Constructional details common to different types of electric apparatus
- H05K7/20—Modifications to facilitate cooling, ventilating, or heating
- H05K7/2029—Modifications to facilitate cooling, ventilating, or heating using a liquid coolant with phase change in electronic enclosures
- H05K7/20336—Heat pipes, e.g. wicks or capillary pumps
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K7/00—Constructional details common to different types of electric apparatus
- H05K7/20—Modifications to facilitate cooling, ventilating, or heating
- H05K7/2029—Modifications to facilitate cooling, ventilating, or heating using a liquid coolant with phase change in electronic enclosures
- H05K7/20381—Thermal management, e.g. evaporation control
-
- 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
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D2015/0291—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes comprising internal rotor means, e.g. turbine driven by the working fluid
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)
Abstract
Description
技术领域Technical field
本发明涉及电子元件散热技术领域,特别涉及一种多源驱动的大功率环路热管散热装置。The invention relates to the technical field of heat dissipation of electronic components, and in particular to a multi-source driven high-power loop heat pipe heat dissipation device.
背景技术Background technique
环路热管传热能力强、热传输距离远、抗重力运行能力强,在高热流密度芯片热管理方面极具前景。但环路热管的最大传热功率受到毛细芯的限制。蒸发器向补偿腔的“漏热”又会引起启动脉冲、温度波动甚至启动失败等问题。现有技术中,通过引射器与环路热管进行耦合的思路,利用引射器的升压特性提供额外的循环驱动力,利用其引射特性解决补偿腔“漏热”问题。Loop heat pipes have strong heat transfer capabilities, long heat transmission distances, and strong anti-gravity operation capabilities. They are very promising in thermal management of high heat flow density chips. However, the maximum heat transfer power of the loop heat pipe is limited by the capillary core. The "heat leakage" of the evaporator to the compensation chamber will cause problems such as starting pulses, temperature fluctuations and even starting failures. In the existing technology, the idea of coupling an ejector to a loop heat pipe is used, and the boost characteristics of the ejector are used to provide additional cycle driving force, and its ejector characteristics are used to solve the problem of "heat leakage" in the compensation cavity.
但是环路热管通过单引射器驱动,在高热流密度下,蒸发器会产生大量蒸汽。由于蒸汽流量受到引射器的蒸汽喷嘴最小截面积的限制,无法快速从蒸发器底板排散,蒸汽槽道内蒸汽分压不断升高,导致高热流密度下底板温度超标,无法满足高功率芯片的散热需求。虽然通过扩大引射器的蒸汽喷嘴的最小截面积(喉部或出口)或增加引射器的数量可以提高蒸汽排出量,降低高功率下的蒸发器底板温度,但也会使得低功率时蒸汽喷嘴出口无法达到音速或超音速,使引射器在低功率运行区间内失去引射和升压性能,严重影响环路热管在低功率下的传热性能和稳定性,无法满足芯片的变负荷运行需求,无法保证大功率设备在小功率下运行。But the loop heat pipe is driven by a single ejector, and under high heat flux density, the evaporator will generate a large amount of steam. Since the steam flow rate is limited by the minimum cross-sectional area of the steam nozzle of the ejector, it cannot be quickly discharged from the evaporator bottom plate. The steam partial pressure in the steam channel continues to increase, causing the bottom plate temperature to exceed the standard under high heat flux density, which cannot meet the requirements of high-power chips. cooling requirements. Although it is possible to increase the steam discharge and reduce the evaporator bottom plate temperature at high power by expanding the minimum cross-sectional area (throat or outlet) of the steam nozzle of the ejector or increasing the number of ejector, it will also make the steam at low power The nozzle outlet cannot reach the speed of sound or supersonic speed, causing the ejector to lose the ejector and boost performance in the low-power operating range, seriously affecting the heat transfer performance and stability of the loop heat pipe at low power, and being unable to meet the variable load of the chip. Operation requirements, it is impossible to guarantee that high-power equipment will operate at low power.
发明内容Contents of the invention
基于此,有必要提供一种多源驱动的大功率环路热管散热装置,能够解决现有技术中的通过单引射器驱动,导致高热流密度下蒸发器的温度超标,无法满足大功率芯片的散热需求的技术问题。Based on this, it is necessary to provide a high-power loop heat pipe cooling device driven by multiple sources, which can solve the problem in the existing technology of being driven by a single ejector, causing the evaporator temperature to exceed the standard under high heat flux density, which cannot meet the needs of high-power chips. technical issues of cooling requirements.
本发明提供的一种多源驱动的大功率环路热管散热装置,用于对芯片进行散热,包括:The invention provides a multi-source driven high-power loop heat pipe cooling device for heat dissipating chips, including:
蒸发器,所述蒸发器用于吸收所述芯片散发的热量,所述蒸发器包括壳体和毛细芯,所述毛细芯能够填充工质,所述壳体具有密封腔体,所述毛细芯设置于所述密封腔体内,并将所述密封腔体隔离成补偿腔和蒸汽槽道,所述蒸汽槽道连接有第一引射器和第二引射器,所述补偿腔分别与所述第一引射器和所述第二引射器连通;Evaporator, the evaporator is used to absorb the heat emitted by the chip, the evaporator includes a shell and a capillary wick, the capillary wick can be filled with working medium, the shell has a sealed cavity, the capillary wick is provided in the sealed cavity, and isolates the sealed cavity into a compensation chamber and a steam channel. The steam channel is connected to a first ejector and a second ejector, and the compensation chamber is connected to the The first ejector is connected to the second ejector;
冷凝器,所述冷凝器的一端分别与所述第一引射器和所述第二引射器连接,另一端与所述补偿腔连通;及A condenser, one end of the condenser is connected to the first ejector and the second ejector respectively, and the other end is connected to the compensation chamber; and
控制组件,所述控制组件分别与所述第二引射器和所述芯片连接,所述控制组件能够根据所述芯片的温度和功率以控制所述第二引射器的通断。A control component, the control component is connected to the second emitter and the chip respectively, and the control component can control the on/off of the second emitter according to the temperature and power of the chip.
进一步地,所述散热装置还包括输送机构,所述输送机构分别与所述补偿腔、所述蒸汽槽道、所述第一引射器、所述第二引射器和所述冷凝器连接,所述输送机构用于供工质和蒸汽在所述补偿腔、所述蒸汽槽道、所述第一引射器、所述第二引射器和所述冷凝器之间循环流动。Further, the heat dissipation device further includes a transport mechanism, which is respectively connected to the compensation chamber, the steam channel, the first ejector, the second ejector and the condenser. , the conveying mechanism is used for circulating working fluid and steam between the compensation chamber, the steam channel, the first ejector, the second ejector and the condenser.
进一步地,所述输送机构包括第一蒸汽管道、第二蒸汽管道、第一液体管道和第二液体管道,所述第一蒸汽管道的一端与所述蒸汽槽道连接,另一端与所述第二液体管道连接,所述第一引射器设置于所述第一蒸汽管道,所述第二蒸汽管道的一端与所述蒸汽槽道连接,另一端与所述第二液体管道连接,所述第二引射器设置于所述第二蒸汽管道,所述第一液体管道的一端与所述补偿腔连通,另一端分别与所述第一引射器和所述第二引射器连接,所述第二液体管道远离所述第一引射器的一端与所述补偿腔连通,所述冷凝器设置于所述第二液体管道。Further, the delivery mechanism includes a first steam pipe, a second steam pipe, a first liquid pipe and a second liquid pipe. One end of the first steam pipe is connected to the steam channel, and the other end is connected to the third steam channel. Two liquid pipes are connected, the first ejector is arranged on the first steam pipe, one end of the second steam pipe is connected to the steam channel, and the other end is connected to the second liquid pipe, the The second ejector is provided in the second steam pipe, one end of the first liquid pipe is connected to the compensation chamber, and the other end is connected to the first ejector and the second ejector respectively, One end of the second liquid pipe away from the first ejector is connected to the compensation chamber, and the condenser is disposed on the second liquid pipe.
进一步地,所述控制组件包括控制器和电磁阀,所述控制器分别与所述电磁阀和所述芯片连接,所述电磁阀与所述第二引射器连接,所述控制器用于根据所述芯片的温度和功率以控制所述电磁阀的开启或关闭,进而以控制所述第二引射器的通断。Further, the control component includes a controller and a solenoid valve, the controller is connected to the solenoid valve and the chip respectively, the solenoid valve is connected to the second ejector, and the controller is used according to The temperature and power of the chip are used to control the opening or closing of the solenoid valve, and further to control the on-off of the second ejector.
进一步地,所述控制组件还包括温度传感器,所述温度传感器分别与所述控制器连接,且所述温度传感器设置于所述芯片上,所述温度传感器用于获取所述芯片的温度信号,并将所述温度信号输送至所述控制器,所述控制器接收所述温度传感器输送的所述温度信号,并根据所述温度信号控制所述电磁阀的开启或关闭。Further, the control component further includes a temperature sensor, the temperature sensor is respectively connected to the controller, and the temperature sensor is arranged on the chip, and the temperature sensor is used to obtain the temperature signal of the chip, And transmit the temperature signal to the controller, the controller receives the temperature signal transmitted by the temperature sensor, and controls the opening or closing of the solenoid valve according to the temperature signal.
进一步地,所述控制器的判断步骤包括:Further, the controller's judgment steps include:
当所述芯片的温度大于第一阈值且所述芯片的功率大于第二阈值时,所述控制器开启所述第二引射器;When the temperature of the chip is greater than the first threshold and the power of the chip is greater than the second threshold, the controller turns on the second emitter;
当所述芯片的温度小于第一阈值且所述芯片的功率大于第二阈值时,所述控制器控制所述第二引射器处于开启状态;When the temperature of the chip is less than the first threshold and the power of the chip is greater than the second threshold, the controller controls the second emitter to be in an open state;
当所述芯片的温度小于第一阈值且所述芯片的功率小于第二阈值时,所述控制器控制所述第二引射器处于关闭状态。When the temperature of the chip is less than the first threshold and the power of the chip is less than the second threshold, the controller controls the second emitter to be in a closed state.
进一步地,所述毛细芯平均孔径小于5μm,由金属粉末烧结而成。Further, the average pore diameter of the capillary core is less than 5 μm and is made of sintered metal powder.
进一步地,所述毛细芯的制备步骤包括:Further, the preparation steps of the capillary core include:
将粒径小于20μm的金属粉末在烘箱干燥后均匀铺展至模具中;The metal powder with a particle size less than 20 μm is evenly spread into the mold after drying in an oven;
在所述金属粉末中混入50~100μm的造孔剂;Mix a 50-100 μm pore-forming agent into the metal powder;
通过压片机对所述模具中的所述金属粉末进行冷压成型,冷压后进行脱模,其中,所述冷压的压力大于200MPa;The metal powder in the mold is cold-pressed and formed by a tablet press, and demolded after cold-pressing, wherein the cold-pressing pressure is greater than 200 MPa;
将脱模之后的中间体放入氮气氛围炉中进行烧结,升温速率为10℃/min,保温30~90min,所述中间体冷却至室温后取出;Put the demolded intermediate into a nitrogen atmosphere furnace for sintering, with a heating rate of 10°C/min and heat preservation for 30 to 90 minutes. The intermediate is cooled to room temperature and then taken out;
将冷却至室温后的所述中间体放入去离子水中超声清洗,对清洗后的中间体进行干燥以形成所述毛细芯。The intermediate after cooling to room temperature is placed in deionized water for ultrasonic cleaning, and the cleaned intermediate is dried to form the capillary core.
进一步地,所述第一引射器包括第一蒸汽喷嘴和第一液体喷嘴,所述第一引射器开设有第一混合腔,所述第一蒸汽喷嘴和所述第一液体喷嘴均与所述第一混合腔相连通,所述蒸汽槽道与所述第一蒸汽喷嘴连通,以使所述蒸汽槽道内的蒸汽能够进入所述第一蒸汽喷嘴,所述第一液体管道与所述第一混合腔所述连通。Further, the first ejector includes a first steam nozzle and a first liquid nozzle, the first ejector is provided with a first mixing chamber, and the first steam nozzle and the first liquid nozzle are connected with each other. The first mixing chamber is connected, the steam channel is connected with the first steam nozzle, so that the steam in the steam channel can enter the first steam nozzle, and the first liquid pipe is connected with the first steam nozzle. The first mixing chamber is connected to the first mixing chamber.
进一步地,所述第一蒸汽喷嘴为渐缩喷嘴。Further, the first steam nozzle is a tapering nozzle.
本发明提供的一种多源驱动的大功率环路热管散热装置,芯片在工作时会产生热量,热量传递至毛细芯,毛细芯内的工质吸收热量后温度上升,形成蒸汽,蒸汽通过蒸汽槽道进入第一引射器和第二引射器,控制组件能够根据芯片温度和功率控制第二引射器的通断。当芯片的温度和功率较高时,控制组件开启第二引射器,通过第一引射器和第二引射器同时工作,能够增加蒸汽的驱动压力,以使蒸发器内的蒸汽能够快速排散,降低蒸发器内的蒸汽分压,从而降低蒸发器内的温度;当芯片的温度和功率较低时,控制组件关闭第二引射器,蒸汽通过第一引射器进入冷凝器,使得低功率时蒸汽喷嘴出口达到音速或超音速,使引射器在低功率运行区间内保持引射和升压性能,保证环路热管在低功率下的传热性能和稳定性,满足芯片的变负荷运行需求,即满足大功率芯片在小功率下运行的散热,从而使得蒸发器的温度能够符合标准,大功率芯片在大功率和小功率运行时都能达到散热需求。The invention provides a multi-source driven high-power loop heat pipe cooling device. The chip generates heat when working, and the heat is transferred to the capillary core. The temperature of the working fluid in the capillary core rises after absorbing the heat, forming steam. The steam passes through the steam. The channel enters the first ejector and the second ejector, and the control component can control the on/off of the second ejector according to the chip temperature and power. When the temperature and power of the chip are high, the control component turns on the second ejector. By working the first ejector and the second ejector simultaneously, the driving pressure of the steam can be increased so that the steam in the evaporator can quickly Discharge, reduce the partial pressure of steam in the evaporator, thereby reducing the temperature in the evaporator; when the temperature and power of the chip are low, the control component closes the second ejector, and the steam enters the condenser through the first ejector. It enables the steam nozzle outlet to reach sonic or supersonic speed at low power, enables the ejector to maintain ejection and boost performance in the low power operating range, ensures the heat transfer performance and stability of the loop heat pipe at low power, and meets the requirements of the chip. The variable load operation requirement is to meet the heat dissipation requirements of high-power chips operating at low power, so that the temperature of the evaporator can meet the standards, and the high-power chip can meet the heat dissipation requirements when operating at high power and low power.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图示出的结构获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the drawings needed to be used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings in the following description are only These are some embodiments of the present invention. For those of ordinary skill in the art, other drawings can be obtained based on the structures shown in these drawings without exerting creative efforts.
图1为本发明实施例的一种多源驱动的大功率环路热管散热装置结构示意图;Figure 1 is a schematic structural diagram of a multi-source driven high-power loop heat pipe cooling device according to an embodiment of the present invention;
图2为本发明实施例的一种多源驱动的大功率环路热管散热装置另一结构示意图;Figure 2 is another structural schematic diagram of a multi-source driven high-power loop heat pipe cooling device according to an embodiment of the present invention;
图3为本发明实施例的控制器的控制方法图;Figure 3 is a control method diagram of the controller according to the embodiment of the present invention;
图4为本发明实施例的毛细芯破泡原理图;Figure 4 is a schematic diagram of capillary core bubble breaking according to an embodiment of the present invention;
图5为本发明实施例的金属粉末烧结毛细芯微观结构图;Figure 5 is a microstructure diagram of a metal powder sintered capillary core according to an embodiment of the present invention;
图6为本发明实施例的金属粉末烧结毛细芯孔径分布图。Figure 6 is a pore size distribution diagram of the metal powder sintered capillary core according to the embodiment of the present invention.
主要元件:Main components:
100、蒸发器;110、壳体;120、毛细芯;130、蒸汽槽道;140、补偿腔;301、毛细弯月面;200、第一引射器;210、第一蒸汽喷嘴;220、第一液体喷嘴;230、第一混合腔;300、第二引射器;310、第一蒸汽喷嘴;320、第二液体喷嘴;330、第二混合腔;400、冷凝器;410、第二翅片;420、风扇;510、控制器;520、电磁阀;530、温度传感器;610、第一蒸汽管道;620、第二蒸汽管道;630、第一液体管道;631、第一翅片;640、第二液体管道;700、芯片;800、热界面材料。100. Evaporator; 110. Shell; 120. Capillary core; 130. Steam channel; 140. Compensation chamber; 301. Capillary meniscus; 200. First ejector; 210. First steam nozzle; 220. First liquid nozzle; 230, first mixing chamber; 300, second ejector; 310, first steam nozzle; 320, second liquid nozzle; 330, second mixing chamber; 400, condenser; 410, second Fin; 420, fan; 510, controller; 520, solenoid valve; 530, temperature sensor; 610, first steam pipe; 620, second steam pipe; 630, first liquid pipe; 631, first fin; 640. Second liquid pipeline; 700. Chip; 800. Thermal interface material.
本发明目的的实现、功能特点及优点将结合实施例,参照附图做进一步说明。The realization of the purpose, functional features and advantages of the present invention will be further described with reference to the embodiments and the accompanying drawings.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明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发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, rather than all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without making creative efforts fall within the scope of protection of the present invention.
需要说明,本发明实施例中所有方向性指示(诸如上、下、左、右、前、后……)仅用于解释在某一特定姿态(如附图所示)下各部件之间的相对位置关系、运动情况等,如果该特定姿态发生改变时,则该方向性指示也相应地随之改变。It should be noted that all directional indications (such as up, down, left, right, front, back...) in the embodiment of the present invention are only used to explain the relationship between components in a specific posture (as shown in the drawings). Relative positional relationship, movement conditions, etc., if the specific posture changes, the directional indication will also change accordingly.
另外,在本发明中涉及“第一”、“第二”等的描述仅用于描述目的,而不能理解为指示或暗示其相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括至少一个该特征。另外,全文中的“和/或”包括三个方案,以A和/或B为例,包括A技术方案、B技术方案,以及A和B同时满足的技术方案;另外,各个实施例之间的技术方案可以相互结合,但是必须是以本领域普通技术人员能够实现为基础,当技术方案的结合出现相互矛盾或无法实现时应当认为这种技术方案的结合不存在,也不在本发明要求的保护范围之内。In addition, descriptions involving "first", "second", etc. in the present invention are for descriptive purposes only and cannot be understood as indicating or implying their relative importance or implicitly indicating the number of indicated technical features. Therefore, features defined as "first" and "second" may explicitly or implicitly include at least one of these features. In addition, "and/or" in the full text includes three solutions, taking A and/or B as an example, including technical solution A, technical solution B, and technical solutions that satisfy both A and B at the same time; in addition, between various embodiments, The technical solutions can be combined with each other, but it must be based on what a person of ordinary skill in the art can realize. When the combination of technical solutions is contradictory or cannot be realized, it should be considered that this combination of technical solutions does not exist and is not required by the present invention. within the scope of protection.
如图1和图2所示,在一些实施例中,一种多源驱动的大功率环路热管散热装置用于对芯片700进行散热,包括蒸发器100、冷凝器400和控制组件,蒸发器100用于吸收芯片700散发的热量,蒸发器100包括壳体110和毛细芯120,毛细芯120能够填充工质,壳体110具有密封腔体,毛细芯120设置于密封腔体内,并将密封腔体隔离成补偿腔140和蒸汽槽道130,蒸汽槽道130连接有第一引射器200和第二引射器300,补偿腔140分别与第一引射器200和第二引射器300连通。冷凝器400的一端分别与第一引射器200和第二引射器300连接,另一端与补偿腔140连通。控制组件分别与第二引射器300和芯片700连接,控制组件能够根据芯片700的温度和功率以控制第二引射器300的通断。As shown in Figures 1 and 2, in some embodiments, a multi-source driven high-power loop heat pipe cooling device is used to dissipate heat from the chip 700, including an evaporator 100, a condenser 400 and a control component. The evaporator 100 is used to absorb the heat emitted by the chip 700. The evaporator 100 includes a shell 110 and a capillary wick 120. The capillary wick 120 can be filled with working medium. The shell 110 has a sealed cavity. The capillary wick 120 is arranged in the sealed cavity and seals it. The cavity is separated into a compensation chamber 140 and a steam channel 130. The steam channel 130 is connected to the first ejector 200 and the second ejector 300. The compensation chamber 140 is connected to the first ejector 200 and the second ejector respectively. 300 connections. One end of the condenser 400 is connected to the first ejector 200 and the second ejector 300 respectively, and the other end is connected to the compensation chamber 140 . The control component is connected to the second emitter 300 and the chip 700 respectively, and the control component can control the on/off of the second emitter 300 according to the temperature and power of the chip 700 .
芯片700在工作时会产生热量,热量传递至毛细芯120,毛细芯120内的工质吸收热量后温度上升,形成蒸汽,蒸汽通过蒸汽槽道130进入第一引射器200和第二引射器300,控制组件能够根据芯片700的温度和功率控制第二引射器300的通断。当芯片700的温度和功率较低时,控制组件关闭第二引射器300,蒸汽通过第一引射器200进入冷凝器400。当芯片700的温度和功率较高时,控制组件开启第二引射器300,通过第一引射器200和第二引射器300同时工作,能够增加蒸汽的驱动压力,以使蒸发器100内的蒸汽能够快速排散,降低蒸发器100内的蒸汽分压,降低蒸发器100内的温度,使得蒸发器100的温度能够符合标准,满足大功率芯片700的散热需求。另外,在大功率芯片工作时,通过第一引射器200和第二引射器300能够大幅提高蒸汽的通流能力,从而使环路热管散热装置能够兼容低沸点工质,不仅拓展环路热管散热装置的应用和存储环境温度范围,还提高环路热管散热装置在使用过程中的安全可靠性,在小功率芯片工作时,第一引射器200和第二引射器同时工作的话,相当于扩大蒸汽喷嘴的截面积,使得蒸汽喷嘴出口出口无法达到音速或超音速,通过控制组件的配合能够实现大功率设备,小功率运行的效果。The chip 700 generates heat when working, and the heat is transferred to the capillary core 120. The temperature of the working fluid in the capillary core 120 rises after absorbing the heat, forming steam. The steam enters the first ejector 200 and the second ejector through the steam channel 130. The control component can control the on/off of the second emitter 300 according to the temperature and power of the chip 700 . When the temperature and power of the chip 700 are low, the control component closes the second ejector 300, and the steam enters the condenser 400 through the first ejector 200. When the temperature and power of the chip 700 are high, the control component turns on the second ejector 300. By working the first ejector 200 and the second ejector 300 at the same time, the driving pressure of the steam can be increased, so that the evaporator 100 The steam in the evaporator can be quickly discharged, reducing the partial pressure of the steam in the evaporator 100 and lowering the temperature in the evaporator 100, so that the temperature of the evaporator 100 can meet the standards and meet the heat dissipation requirements of the high-power chip 700. In addition, when the high-power chip is working, the flow capacity of steam can be greatly improved through the first ejector 200 and the second ejector 300, so that the loop heat pipe heat dissipation device can be compatible with low boiling point working fluids, which not only expands the loop The application and storage environment temperature range of the heat pipe heat dissipation device also improves the safety and reliability of the loop heat pipe heat dissipation device during use. When the low-power chip is working, if the first injector 200 and the second injector work at the same time, It is equivalent to expanding the cross-sectional area of the steam nozzle so that the outlet of the steam nozzle cannot reach the speed of sound or supersonic speed. Through the cooperation of the control components, the effect of high-power equipment and low-power operation can be achieved.
再者,环路热管散热装置要满足高低温环境(-40~+40℃)存放和运行要求,民用领域还要求工质无毒、不易燃。其中对高低温存放的要求把水这一换热性能优良的工质排除,而无毒且不易燃的要求则排除了醇类和氨类工质。低沸点工质(如电子氟化液HFE7100、FC72,氟利昂R134a、R22等)能够同时满足上述要求。然而,低沸点工质的汽化潜热一般在水工质的1/10~1/20范围,在同样的散热功率下,低沸点工质将产生大量蒸汽,单引射器方案将无法满足蒸汽通流和排散需求,易导致蒸发器100温度急剧升高。Furthermore, the loop heat pipe cooling device must meet the storage and operation requirements in high and low temperature environments (-40 ~ +40°C). The civilian field also requires that the working fluid is non-toxic and non-flammable. Among them, the requirements for high and low temperature storage exclude water, a working fluid with excellent heat exchange performance, while the non-toxic and non-flammable requirements exclude alcohol and ammonia working fluids. Low boiling point working fluids (such as electronic fluorinated fluid HFE7100, FC72, Freon R134a, R22, etc.) can meet the above requirements at the same time. However, the latent heat of vaporization of low-boiling-point working fluids is generally in the range of 1/10 to 1/20 of that of water working fluids. Under the same heat dissipation power, low-boiling point working fluids will generate a large amount of steam, and the single ejector solution will not be able to meet the steam flow requirements. Flow and dissipation requirements may easily cause the temperature of the evaporator 100 to rise sharply.
另外,本申请的多源驱动的大功率环路热管散热装置能够大幅提高蒸汽通流能力,从而能够兼容低沸点工质,不仅拓展了环路热管的应用和存储环境温度范围,还提高了环路热管散热装置在使用过程中的安全可靠性(低沸点工质具有高绝缘性、无毒且不可燃等优点)。In addition, the multi-source driven high-power loop heat pipe cooling device of this application can greatly improve the steam flow capacity and is therefore compatible with low boiling point working fluids. It not only expands the application and storage environment temperature range of the loop heat pipe, but also improves the environmental protection. The safety and reliability of the heat pipe heat dissipation device during use (low boiling point working fluid has the advantages of high insulation, non-toxic and non-flammable).
本申请的一种多源驱动的大功率环路热管散热装置,在芯片700的低功率下仅开启第一引射器200,保证环路热管在芯片700的低功率下的传热性和稳定性。在芯片700高功率下开启第二引射器300,使得蒸汽和冷液的流量都得到大幅度提升,从而有效提高环路热管的传热极限和高功率芯片700下的散热性能。因此,本申请所述一种多源驱动的大功率环路热管能够满足大功率芯片700的变负荷运行散热需求。A multi-source driven high-power loop heat pipe heat dissipation device of this application only turns on the first ejector 200 when the chip 700 is at low power, ensuring the heat transfer and stability of the loop heat pipe under the low power of the chip 700 sex. When the second ejector 300 is turned on when the chip 700 is at high power, the flow rates of steam and cold liquid are greatly increased, thereby effectively improving the heat transfer limit of the loop heat pipe and the heat dissipation performance of the high-power chip 700 . Therefore, the multi-source driven high-power loop heat pipe described in this application can meet the heat dissipation requirements of the high-power chip 700 during variable load operation.
具体地,散热装置还包括输送机构,输送机构分别与补偿腔140、蒸汽槽道130、第一引射器200、第二引射器300和冷凝器400连接,输送机构用于供工质和蒸汽在补偿腔140、蒸汽槽道130、第一引射器200、第二引射器300和冷凝器400之间循环流动。Specifically, the heat dissipation device also includes a conveying mechanism, which is respectively connected to the compensation chamber 140, the steam channel 130, the first ejector 200, the second ejector 300 and the condenser 400. The conveying mechanism is used to supply working fluid and Steam circulates between the compensation chamber 140, the steam channel 130, the first ejector 200, the second ejector 300 and the condenser 400.
更具体地,输送机构包括第一蒸汽管道610、第二蒸汽管道620、第一液体管道630和第二液体管道640,第一蒸汽管道610的一端与蒸汽槽道130连接,另一端与第二液体管道640连接,第一引射器200设置于第一蒸汽管道610,第二蒸汽管道620的一端与蒸汽槽道130连接,另一端与第二液体管道640连接,第二引射器300设置于第二蒸汽管道620,第一液体管道630的一端与补偿腔140连通,另一端分别与第一引射器200和第二引射器300连接,第二液体管道640远离第一引射器200的一端与补偿腔140连通,冷凝器400设置于第二液体管道640。具体地,第一液体管道630上还设置有第一翅片631。More specifically, the delivery mechanism includes a first steam pipe 610, a second steam pipe 620, a first liquid pipe 630 and a second liquid pipe 640. One end of the first steam pipe 610 is connected to the steam channel 130, and the other end is connected to the second steam channel 130. The liquid pipe 640 is connected, the first ejector 200 is disposed in the first steam pipe 610, one end of the second steam pipe 620 is connected to the steam channel 130, and the other end is connected to the second liquid pipe 640, and the second ejector 300 is disposed In the second steam pipe 620, one end of the first liquid pipe 630 is connected to the compensation chamber 140, and the other end is connected to the first ejector 200 and the second ejector 300 respectively. The second liquid pipe 640 is away from the first ejector. One end of 200 is connected to the compensation chamber 140, and the condenser 400 is disposed in the second liquid pipe 640. Specifically, the first fin 631 is also provided on the first liquid pipe 630 .
工作时,蒸汽槽道130内的蒸汽同时进入第一蒸汽管道610和第二蒸汽管道620,并分别进入第一引射器200和第二引射器300,补偿腔140内的冷液通过第一液体管道630分别进入第一引射器200和第二引射器300,蒸发通过第一引射器200和第二引射器300加压形成高速蒸汽,高速蒸汽与冷液在第一引射器200和第二引射器300内混合后形成超音速气液两相流,并在第一引射器200和第二引射器300内形成凝结激波,以使从第一引射器200和第二引射器300出来的是高压热液体,高压热液体分别从第一蒸汽管道610和第二蒸汽管道620汇合进入第二液体管道640,并经过冷凝器400进行冷凝后形成冷液,冷液流入补偿腔140内。流入补偿腔140的冷液大部分在第一引射器200和第二引射器300的抽吸下流入第一引射器200和第二引射器300,并吸收热量和带走毛细芯120上表面气泡。小部分冷液在毛细力和重力的作用下穿过毛细芯120,成为毛细芯120的填充工质,在芯片700散发的热量作用下毛细芯120内的工质蒸发成蒸汽,以使蒸汽和液体在补偿腔140、蒸发槽道、第一引射器200、第二引射器300和冷凝器400之间循环流动。During operation, the steam in the steam channel 130 enters the first steam pipe 610 and the second steam pipe 620 at the same time, and enters the first ejector 200 and the second ejector 300 respectively. The cold liquid in the compensation chamber 140 passes through the first ejector 200 and the second ejector 300 . A liquid pipe 630 enters the first ejector 200 and the second ejector 300 respectively. The evaporation is pressurized through the first ejector 200 and the second ejector 300 to form high-speed steam. The high-speed steam and cold liquid are evaporated in the first ejector 200 and the second ejector 300. After mixing in the ejector 200 and the second ejector 300, a supersonic gas-liquid two-phase flow is formed, and a condensation shock wave is formed in the first ejector 200 and the second ejector 300, so that from the first ejector The high-pressure hot liquid comes out of the ejector 200 and the second ejector 300. The high-pressure hot liquid merges from the first steam pipe 610 and the second steam pipe 620 into the second liquid pipe 640, and is condensed through the condenser 400 to form cold water. Liquid, cold liquid flows into the compensation chamber 140. Most of the cold liquid flowing into the compensation chamber 140 flows into the first ejector 200 and the second ejector 300 under the suction of the first ejector 200 and the second ejector 300, and absorbs heat and takes away the capillary core. 120 bubbles on the upper surface. A small part of the cold liquid passes through the capillary core 120 under the action of capillary force and gravity, and becomes the filling working fluid of the capillary core 120. Under the action of the heat emitted by the chip 700, the working fluid in the capillary core 120 evaporates into steam, so that the steam and The liquid circulates between the compensation chamber 140, the evaporation channel, the first ejector 200, the second ejector 300 and the condenser 400.
具体地,冷凝器400为蛇形管冷凝器。第二液体管道640上还设置有第二翅片410和风扇420,以增加冷凝器400的冷凝效果。蒸发器100的底部与芯片700通过热界面材料800紧密贴合。更具体地,第一引射器200与第二引射器300的结构相同。Specifically, the condenser 400 is a serpentine condenser. The second liquid pipe 640 is also provided with a second fin 410 and a fan 420 to increase the condensation effect of the condenser 400 . The bottom of the evaporator 100 is closely connected to the chip 700 through the thermal interface material 800 . More specifically, the first ejector 200 and the second ejector 300 have the same structure.
进一步地,第一引射器200包括第一蒸汽喷嘴210和第一液体喷嘴220,第一引射器200开设有第一混合腔230,第一蒸汽喷嘴210和第一液体喷嘴220均与第一混合腔230相连通,第一液体喷嘴220设置于第一蒸汽喷嘴210的外侧,蒸汽槽道130与第一蒸汽喷嘴210连通,以使蒸汽槽道130内的蒸汽能够进入第一蒸汽喷嘴210,第一液体管道630与第一混合腔230连通。Further, the first injector 200 includes a first steam nozzle 210 and a first liquid nozzle 220. The first injector 200 is provided with a first mixing chamber 230. The first steam nozzle 210 and the first liquid nozzle 220 are both connected with the first mixing chamber 230. A mixing chamber 230 is connected, the first liquid nozzle 220 is arranged outside the first steam nozzle 210, and the steam channel 130 is connected with the first steam nozzle 210, so that the steam in the steam channel 130 can enter the first steam nozzle 210 , the first liquid pipe 630 is connected with the first mixing chamber 230 .
更进一步地,第二引射器300包括第二蒸汽喷嘴310和第二液体喷嘴320,第二引射器300开设有第二混合腔330,第二蒸汽喷嘴310和第二液体喷嘴320均与第二混合腔330相连通,第二液体喷嘴320设置于第二蒸汽喷嘴310的外侧,蒸汽槽道130与第二蒸汽喷嘴310连通,以使蒸汽槽道130内的蒸汽能够进入第二蒸汽喷嘴310,第二液体管道640与第二混合腔330连通。Furthermore, the second injector 300 includes a second steam nozzle 310 and a second liquid nozzle 320. The second injector 300 is provided with a second mixing chamber 330. The second steam nozzle 310 and the second liquid nozzle 320 are both connected with The second mixing chamber 330 is connected, the second liquid nozzle 320 is arranged outside the second steam nozzle 310, and the steam channel 130 is connected with the second steam nozzle 310, so that the steam in the steam channel 130 can enter the second steam nozzle. 310. The second liquid pipe 640 is connected with the second mixing chamber 330.
进一步地,第一蒸汽喷嘴210和第二蒸汽喷嘴310优选为渐缩喷嘴,其目的在于防止蒸汽在膨胀过程中冷凝而影响环路热管散热性能,主要原因是:蒸发器100所产生的蒸汽一般为饱和态,如采用传统以蒸汽为一次流体、蒸汽喷嘴为缩放结构的引射器,饱和蒸汽流经缩放喷嘴的喉部以后,在扩张段极有可能因激波产生而出现过冷,使部分蒸汽在蒸汽喷嘴内冷凝,极大地影响引射器性能,进而影响环路热管性能。Furthermore, the first steam nozzle 210 and the second steam nozzle 310 are preferably tapered nozzles. The purpose is to prevent the steam from condensing during the expansion process and affecting the heat dissipation performance of the loop heat pipe. The main reason is that the steam generated by the evaporator 100 is generally is in a saturated state. For example, if a traditional ejector with steam as the primary fluid and a steam nozzle as a scaling structure is used, after the saturated steam flows through the throat of the scaling nozzle, it is very likely that supercooling will occur in the expansion section due to the generation of shock waves, causing the Part of the steam condenses in the steam nozzle, which greatly affects the performance of the ejector and thus the loop heat pipe.
进一步地,控制组件包括控制器510和电磁阀520,控制器510分别与电磁阀520和芯片700连接,电磁阀520与第二引射器300连接,电磁阀520设置于第二蒸汽管道620上,且位于蒸汽槽道130和第二引射器300之间,控制器510用于根据芯片700的温度和功率以控制电磁阀520的开启或关闭,进而以控制第二引射器300的通断。具体地,控制器510可以但不限于为PID控制器510。Further, the control component includes a controller 510 and a solenoid valve 520. The controller 510 is connected to the solenoid valve 520 and the chip 700 respectively. The solenoid valve 520 is connected to the second ejector 300. The solenoid valve 520 is disposed on the second steam pipe 620. , and is located between the steam channel 130 and the second ejector 300. The controller 510 is used to control the opening or closing of the solenoid valve 520 according to the temperature and power of the chip 700, thereby controlling the passage of the second ejector 300. Break. Specifically, the controller 510 may be, but is not limited to, a PID controller 510.
更进一步地,控制组件还包括温度传感器530,温度传感器530分别与控制器510连接,且温度传感器530设置于芯片700上,温度传感器530用于获取芯片700的温度信号,并将温度信号输送至控制器510,控制器510接收温度传感器530输送的温度信号,并根据温度信号控制电磁阀520的开启或关闭。具体地,温度传感器530可以设置为多个,多个温度传感器530同时获取芯片700的温度信号,并取其平均值,从而提高温度测量的准确度。优选地,温度传感器530可以设置为两个。Furthermore, the control component also includes a temperature sensor 530. The temperature sensor 530 is connected to the controller 510 respectively. The temperature sensor 530 is disposed on the chip 700. The temperature sensor 530 is used to obtain the temperature signal of the chip 700 and transmit the temperature signal to Controller 510. The controller 510 receives the temperature signal transmitted by the temperature sensor 530, and controls the opening or closing of the solenoid valve 520 according to the temperature signal. Specifically, multiple temperature sensors 530 may be provided, and the multiple temperature sensors 530 simultaneously obtain the temperature signals of the chip 700 and average them, thereby improving the accuracy of temperature measurement. Preferably, two temperature sensors 530 may be provided.
在一些实施例中,控制器510的判断步骤包括:In some embodiments, the determination steps of the controller 510 include:
当芯片700的温度大于第一阈值且芯片700的功率大于第二阈值时,控制器510开启第二引射器300;When the temperature of the chip 700 is greater than the first threshold and the power of the chip 700 is greater than the second threshold, the controller 510 turns on the second emitter 300;
当芯片700的温度小于第一阈值且芯片700的功率大于第二阈值时,控制器510控制第二引射器300处于开启状态;When the temperature of the chip 700 is less than the first threshold and the power of the chip 700 is greater than the second threshold, the controller 510 controls the second ejector 300 to be in an on state;
当芯片700的温度小于第一阈值且芯片700的功率小于第二阈值时,控制器510控制第二引射器300处于关闭状态。其中,第一阈值为85℃。When the temperature of the chip 700 is less than the first threshold and the power of the chip 700 is less than the second threshold, the controller 510 controls the second emitter 300 to be in a closed state. Among them, the first threshold is 85°C.
如图3所示,具体地,当芯片700的发热功率Q大于第二阈值Q1,第一温度传感器530所测温度T1和第二温度传感器530所测温度T2的算数平均值Tave>85℃时,PID控制器510发出脉冲信号,使电磁阀520开启,第一引射器200和第二引射器300同时工作,环路热管散热装置进入双引射器工作模式,蒸汽通流能力大幅提高,使芯片700的温度迅速降低。当Tave<85℃,Q>Q1时,PID控制器510继续动作,维持电磁阀520在常开状态。当Tave<85℃,Q<Q1时,PID控制器510不发出脉冲信号,维持阀门9在常闭状态,第一引射器200开启,第二引射器300关闭,环路热管散热装置进入单引射器工作模式。As shown in Figure 3, specifically, when the heating power Q of the chip 700 is greater than the second threshold Q1, and the arithmetic mean Tave of the temperature T1 measured by the first temperature sensor 530 and the temperature T2 measured by the second temperature sensor 530 is >85°C , the PID controller 510 sends a pulse signal to open the solenoid valve 520, the first ejector 200 and the second ejector 300 work at the same time, the loop heat pipe cooling device enters the dual ejector working mode, and the steam flow capacity is greatly improved. , causing the temperature of the chip 700 to drop rapidly. When Tave<85°C and Q>Q1, the PID controller 510 continues to operate and maintains the solenoid valve 520 in the normally open state. When Tave<85℃, Q<Q1, the PID controller 510 does not send out a pulse signal and maintains the valve 9 in a normally closed state. The first ejector 200 is opened, the second ejector 300 is closed, and the loop heat pipe cooling device enters Single emitter working mode.
PID控制器510的数学表达式为The mathematical expression of PID controller 510 is
式(1)中:e(t)为系统偏差,Kp为比例控制参数,KI为积分控制参数,Kd为微分控制参数。三个参数要根据实际环路热管散热装置来进行优化选取。In formula (1): e(t) is the system deviation, Kp is the proportional control parameter, KI is the integral control parameter, and Kd is the differential control parameter. The three parameters should be optimized and selected based on the actual loop heat pipe cooling device.
进一步地,PID控制器510的反馈回路中,输入信号为芯片700平均温度Teva和发热功率Q,输出信号为控制电磁阀520开启或开闭的脉冲电信号。Further, in the feedback loop of the PID controller 510, the input signal is the average temperature Teva and the heating power Q of the chip 700, and the output signal is a pulse electrical signal that controls the opening or closing of the solenoid valve 520.
如图4所示,低沸点工质往往表面张力较低(约为水的1/4~1/5),根据Young-Laplace方程(式2),在使用同样的毛细芯120时(有效孔径相同),其“破泡压力”远低于水,部分蒸汽容易穿过毛细芯120而进入补偿腔140,使蒸发器100无法实现气液相分离,且易引发启动脉冲、温度波动和启动失败等问题。低沸点绝缘液的毛细力较低,这意味着当工质在毛细芯120的孔隙间相变时,毛细弯月面301液体侧的压头较小。在加热功率高时,气侧分压高于液体侧分压(即毛细压头),毛细弯月面301将向补偿腔140移动,形成“破泡”现象。“破泡”使得补偿腔140压力和温度升高,影响液体回流,最终导致环路热管无法启动。As shown in Figure 4, low-boiling point working fluids tend to have lower surface tension (about 1/4 to 1/5 of water). According to the Young-Laplace equation (Equation 2), when using the same capillary core 120 (effective pore diameter Same), its "bubble breaking pressure" is much lower than that of water, and part of the steam easily passes through the capillary wick 120 and enters the compensation chamber 140, making it impossible for the evaporator 100 to achieve gas-liquid phase separation, and easily causing startup pulses, temperature fluctuations and startup failures. And other issues. The capillary force of the low boiling point insulating liquid is lower, which means that when the working fluid changes phase between the pores of the capillary core 120, the pressure head on the liquid side of the capillary meniscus 301 is smaller. When the heating power is high, the gas side partial pressure is higher than the liquid side partial pressure (ie, capillary head), and the capillary meniscus 301 will move toward the compensation chamber 140, forming a "bubble breaking" phenomenon. "Bubble breaking" causes the pressure and temperature of the compensation chamber 140 to increase, which affects the liquid return flow and ultimately causes the loop heat pipe to fail to start.
式(2)中:△P—破泡压力,kPa;σ—表面张力,N/m;θ—接触角;reff—毛细芯120有效孔径,m。In formula (2): △P—bubble breaking pressure, kPa; σ—surface tension, N/m; θ—contact angle; r eff —capillary core 120 effective pore diameter, m.
在一些实施例中,毛细芯120平均孔径小于5μm,由金属粉末烧结而成。根据式(2),小孔径毛细芯120能够产生较大的毛细压头,有效防止“破泡”现象,使低沸点、低表面张力工质能够适用于环路热管。In some embodiments, the capillary core 120 has an average pore diameter less than 5 μm and is made of sintered metal powder. According to formula (2), the small-pore capillary core 120 can generate a larger capillary pressure head, effectively preventing the "bubble breaking" phenomenon, making the low boiling point and low surface tension working fluid suitable for loop heat pipes.
具体地,毛细芯120的制备步骤包括:Specifically, the preparation steps of the capillary core 120 include:
S1、将粒径小于20μm的金属粉末在烘箱干燥后均匀铺展至模具中。其中,金属粉末的材质可以是铜、镍或不锈钢等。S1. Evenly spread the metal powder with a particle size less than 20 μm into the mold after drying in the oven. Among them, the material of the metal powder can be copper, nickel or stainless steel.
S2、在金属粉末中混入50~100μm的造孔剂,以提高金属粉末烧结毛细芯120的孔隙率。其中,造孔剂为NaCl或Na2CO3等易溶于水的盐类。S2. Mix a 50-100 μm pore-forming agent into the metal powder to increase the porosity of the metal powder sintered capillary core 120. Among them, the pore-forming agent is a salt that is easily soluble in water such as NaCl or Na 2 CO 3 .
S3、通过压片机对模具中的金属粉末进行冷压成型,冷压后进行脱模,以保证毛细芯120具有较小的有效孔径。其中,冷压的压力大于200MPa。S3. Use a tablet press to cold-press the metal powder in the mold, and then demould after cold-pressing to ensure that the capillary core 120 has a smaller effective aperture. Among them, the pressure of cold pressing is greater than 200MPa.
S4、将脱模之后的中间体放入氮气氛围炉中进行烧结,升温速率为10℃/min,保温30~90min,中间体冷却至室温后取出。S4. Put the demolded intermediate into a nitrogen atmosphere furnace for sintering. The heating rate is 10°C/min, and the temperature is maintained for 30 to 90 minutes. The intermediate is cooled to room temperature and then taken out.
S5、将冷却至室温后的中间体放入去离子水中超声清洗,对清洗后的中间体进行干燥以形成毛细芯120。S5. Put the intermediate cooled to room temperature into deionized water for ultrasonic cleaning, and dry the cleaned intermediate to form the capillary core 120.
如图5和图6所示,上述制备步骤制备的小孔径金属粉末烧结毛细芯120具有致密的孔结构,经统计其有效孔径低于5μm,大部分微孔直径分布在1~2μm区间,能够提供较大的毛细压头,延缓“破泡”现象。As shown in Figures 5 and 6, the small-pore metal powder sintered capillary core 120 prepared by the above preparation steps has a dense pore structure. According to statistics, its effective pore diameter is less than 5 μm, and most of the micropore diameters are distributed in the range of 1 to 2 μm, which can Provide a larger capillary pressure head and delay the "bubble breaking" phenomenon.
以上所述仅为本发明的优选实施例,并非因此限制本发明的专利范围,凡是在本发明的发明构思下,利用本发明说明书及附图内容所作的等效结构变换,或直接/间接运用在其他相关的技术领域均包括在本发明的专利保护范围内。The above are only preferred embodiments of the present invention, and do not limit the patent scope of the present invention. Under the inventive concept of the present invention, equivalent structural transformations can be made using the contents of the description and drawings of the present invention, or direct/indirect applications. Other related technical fields are included in the patent protection scope of the present invention.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210949782.8A CN115307469B (en) | 2022-08-09 | 2022-08-09 | Multi-source driven high-power loop heat pipe radiating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210949782.8A CN115307469B (en) | 2022-08-09 | 2022-08-09 | Multi-source driven high-power loop heat pipe radiating device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN115307469A CN115307469A (en) | 2022-11-08 |
| CN115307469B true CN115307469B (en) | 2024-03-22 |
Family
ID=83860734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210949782.8A Active CN115307469B (en) | 2022-08-09 | 2022-08-09 | Multi-source driven high-power loop heat pipe radiating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115307469B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102359745A (en) * | 2011-07-06 | 2012-02-22 | 罗勰 | Moderate and low temperature mixed working medium thermal and electrical combined cycle based on brown cycle |
| DE202017100039U1 (en) * | 2017-01-06 | 2017-03-14 | Shanghai Ocean University | Jet self-cascade refrigeration system for residual heat recovery of a tuna fishing boat |
| CN112179188A (en) * | 2020-09-25 | 2021-01-05 | 西安交通大学 | A flat-plate loop heat pipe capable of stable operation under high heat leakage and using method |
| CN114772674A (en) * | 2022-05-09 | 2022-07-22 | 南京工业大学 | Low-carbon running saline wastewater treatment system and method applying solar energy and loop heat pipe |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109855456B (en) * | 2019-03-12 | 2020-06-19 | 西安交通大学 | Loop heat pipe radiator with vapor-liquid two-phase flow jet boosting device |
-
2022
- 2022-08-09 CN CN202210949782.8A patent/CN115307469B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102359745A (en) * | 2011-07-06 | 2012-02-22 | 罗勰 | Moderate and low temperature mixed working medium thermal and electrical combined cycle based on brown cycle |
| DE202017100039U1 (en) * | 2017-01-06 | 2017-03-14 | Shanghai Ocean University | Jet self-cascade refrigeration system for residual heat recovery of a tuna fishing boat |
| CN112179188A (en) * | 2020-09-25 | 2021-01-05 | 西安交通大学 | A flat-plate loop heat pipe capable of stable operation under high heat leakage and using method |
| CN114772674A (en) * | 2022-05-09 | 2022-07-22 | 南京工业大学 | Low-carbon running saline wastewater treatment system and method applying solar energy and loop heat pipe |
Also Published As
| Publication number | Publication date |
|---|---|
| CN115307469A (en) | 2022-11-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111642103B (en) | High heat flux porous heat sink flow cooling device | |
| CN205262267U (en) | Flat loop heat pipe cooling ware system | |
| CN112201635A (en) | Cooperatively driven high-heat-flux-density chip phase-change heat dissipation device and method | |
| CN103687455A (en) | A vacuum chamber vapor chamber | |
| CN208523114U (en) | Cold plate and refrigeration system with it | |
| CN113357946B (en) | Self-driven thermosiphon loop heat dissipation device of coupled gas-liquid two-phase flow ejector pump | |
| CN101944702A (en) | Two-fluid nozzle atomizing cooling closed system for high-power solid laser | |
| CN113624046B (en) | A kind of array fin type condensing device and loop heat pipe | |
| CN104089509A (en) | Capillary pumped loop | |
| CN100566530C (en) | Micro droplet cooling device | |
| CN102514733A (en) | Microgravity environment-based spray cooling loop device | |
| CN112000206A (en) | Heat radiation system based on pump-driven capillary phase change loop | |
| CN108444320A (en) | A kind of jet chimney width is more than the flat-plate minitype loop circuit heat pipe of fluid pipeline width | |
| CN112696961B (en) | Three-stage phase change heat exchanger | |
| CN115307469B (en) | Multi-source driven high-power loop heat pipe radiating device | |
| CN102853701A (en) | Evaporator for loop heat pipe and application of evaporator | |
| CN114883683A (en) | High-power lithium ion power battery pack spray cooling system and cooling method thereof | |
| CN107094360B (en) | A Flat Micro Loop Heat Pipe System | |
| CN107094361B (en) | A flat micro-circulation heat pipe with an upper cover plate and a chamber | |
| CN111263565B (en) | A cooling device and its working method | |
| CN209978680U (en) | Double-taper micro-channel radiator with thermosyphon loop | |
| CN102954718A (en) | Spray type heat pipe exchanger and method thereof | |
| CN116834956B (en) | Aircraft thermal management integrated system based on low-pressure flash evaporation spray technology | |
| CN219018121U (en) | Flash evaporation heat dissipation system and high-power fiber laser equipment | |
| CN107087375B (en) | The flat type loop heat pipe that a kind of vaporization chamber does not connect directly with jet chimney |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |