WO2017046986A1 - Cooling device and electronic device equipped with same - Google Patents
Cooling device and electronic device equipped with same Download PDFInfo
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- WO2017046986A1 WO2017046986A1 PCT/JP2016/003328 JP2016003328W WO2017046986A1 WO 2017046986 A1 WO2017046986 A1 WO 2017046986A1 JP 2016003328 W JP2016003328 W JP 2016003328W WO 2017046986 A1 WO2017046986 A1 WO 2017046986A1
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- heat
- heat receiving
- path
- return
- receiver
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- 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
Definitions
- the present invention relates to a cooling device for cooling an electronic component and an electronic apparatus equipped with the cooling device.
- a conventional cooling device 110 includes a housing 112 that is a heat receiving portion, and the housing 112 includes an inlet 114 through which a refrigerant flows, an outlet 116 through which a refrigerant flows, and a pipe. And a road portion 130.
- an evaporator section 132 and a circulation section 134 are provided adjacent to each other.
- the refrigerant flowing from the inlet 114 is vaporized by the heat of the inverter 108, which is a heating element.
- the vaporized refrigerant flows through the flow part 134 and flows out from the outlet 116.
- the evaporator part 132 is provided with a plurality of fins 140 that protrude from the bottom wall part 120 toward the flow part 134.
- circulates the clearance gap between the some fin 140 (for example, refer patent document 1).
- the inverter 108 since the inverter 108 is installed horizontally on the bottom surface of the housing 112, the bottom wall portion 120 of the housing 112 is filled with a liquid-phase refrigerant.
- the refrigerant flows through the gaps between the plurality of fins 140 protruding from the bottom wall part 120 toward the flow part 134.
- the plurality of inverters 108 are cooled by increasing the distance from the inlet 114 to the outlet 116 of the casing 112 having such a configuration.
- the cooling device 110 becomes a state where the inverter 108 cannot be cooled. This state is a so-called dry-out state. In this state, the temperature of the inverter 108 increases.
- the cooling device according to the present invention is configured such that the liquid phase refrigerant reaches the most downstream side on the return path side of the heat receiving portion. Thereby, the downstream dryout of the heat receiving part on the return path side is suppressed. That is, the cooling device according to the present invention does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
- a cooling device is a cooling device that cools a heating element by a phase change of a refrigerant, and sequentially connects a heat receiving unit, a heat radiation path, a heat radiation unit, and a return path.
- a circulation path for the formed refrigerant is provided.
- the heat receiving part has a horizontally long rectangular parallelepiped shape with a front surface and a rear surface having a maximum area, a heat receiving plate, a heat dissipation internal path, a return internal path, a fin portion having a plurality of flat fins, an outlet, and an inlet And one or a plurality of partition walls, a plurality of heat receivers, a heat dissipation internal path opening, and a return internal path opening.
- the heat receiving plate is provided with a plurality of heating elements on at least one of the front surface and the rear surface.
- the heat dissipation internal path is provided in the upper part of the heat receiving part, and the refrigerant flows through the heat dissipation internal path.
- the return internal path is provided below the heat receiving part, and the refrigerant flows through the return internal path.
- the fin portion is provided between the heat dissipation internal path and the return internal path.
- the outflow port connects the heat dissipation path and the heat dissipation internal path.
- the inflow port connects the return path and the return internal path.
- the partition wall is provided between the front surface and the rear surface of the heat receiving unit so as to be parallel to the fins.
- the heat receiver is formed by being surrounded by the partition wall and the inner wall of the heat receiving portion.
- the heat radiation internal path opening communicates the heat radiation internal path of each heat receiver in the partition wall.
- the return internal path opening communicates the return internal path of each heat receiver in the partition wall.
- the inflow port and the outflow port are provided on the same side surface of the heat receiving unit.
- the fin portion protrudes inward from the heat receiving plate, and is provided so that the refrigerant flow path constituted by the gap between the fins is in the vertical direction.
- the calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is smaller than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate. This achieves the intended purpose.
- the cooling device is a cooling device that cools a heating element by a phase change of the refrigerant, and is a refrigerant that is formed by sequentially connecting a heat receiving part, a heat radiation path, a heat radiation part, and a return path. Provide a circulation path.
- the heat receiving part has a horizontally long rectangular parallelepiped shape with a front surface and a rear surface having a maximum area, a heat receiving plate, a heat dissipation internal path, a return internal path, a fin portion having a plurality of flat fins, an outlet, and an inlet And one or a plurality of partition walls, a plurality of heat receivers, a heat dissipation internal path opening, and a return internal path opening.
- the heat receiving plate is provided with a plurality of heating elements on at least one of the front surface and the rear surface.
- the heat dissipation internal path is provided in the upper part of the heat receiving part, and the refrigerant flows through the heat dissipation internal path.
- the return internal path is provided below the heat receiving part, and the refrigerant flows through the return internal path.
- the fin portion is provided between the heat dissipation internal path and the return internal path.
- the outflow port connects the heat dissipation path and the heat dissipation internal path.
- the inflow port connects the return path and the return internal path.
- the partition wall is provided between the front surface and the rear surface of the heat receiving unit so as to be parallel to the fins.
- the heat receiver is formed by being surrounded by the partition wall and the inner wall of the heat receiving portion.
- the heat radiation internal path opening communicates the heat radiation internal path of each heat receiver in the partition wall.
- the return internal path opening communicates the return internal path of each heat receiver in the partition wall.
- the inflow port and the outflow port are provided on the same side surface of the heat receiving unit.
- the fin portion protrudes inward from the heat receiving plate, and is provided so that the refrigerant flow path constituted by the gap between the fins is in the vertical direction.
- the calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is smaller than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate. In this way, the liquid-phase refrigerant spreads to the most downstream side on the return path side of the heat receiving portion. Thereby, the downstream dryout of the heat receiving part on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
- the liquid-phase refrigerant in the return path flows into the return internal path from the inflow port, and flows out from the return internal path to the fin portion. Then, the liquid-phase refrigerant that has flowed out to the fin portion receives heat generated from the heating element via the fins, becomes a two-phase refrigerant of a gas phase and a liquid phase, and is in a high pressure state. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
- the heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is configured to be smaller than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate. Therefore, the temperature of the most downstream heat receiver is lower than the temperature of the upstream heat receiver. Therefore, in the most downstream heat receiver, since the amount of heat received by the refrigerant is smaller than that of the upstream heat receiver, the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant is also small. Accordingly, the pressure in the most downstream heat receiver is lower than the pressure in the upstream heat receiver. The refrigerant easily flows to the downstream most downstream heat receiver. Therefore, dryout is suppressed in the downstream heat receiver on the return path side.
- the calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is larger than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate.
- the structure is also small. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
- FIG. 1 is a schematic view of an electronic apparatus equipped with the cooling device according to the first embodiment of the present invention.
- FIG. 2 is a view showing an appearance of a heat receiving portion of the cooling device.
- FIG. 3 is an exploded perspective view of a heat receiving portion of the cooling device.
- FIG. 4 is an exploded perspective view of a heat receiving portion of the cooling device.
- FIG. 5 is a view seen from the front side with the heat receiving plate on the front side of the heat receiving unit of the cooling device removed.
- FIG. 6 is an exploded perspective view of the heat receiving portion of the cooling device according to the second embodiment of the present invention.
- FIG. 7 is a view seen from the front side with the heat receiving plate on the front side of the heat receiving unit of the cooling device removed.
- FIG. 8 is a schematic view showing a conventional cooling device.
- a cooling device is a cooling device that cools a heating element by a phase change of the refrigerant, and circulates the refrigerant formed by sequentially connecting a heat receiving part, a heat radiation path, a heat radiation part, and a return path. Provide a route.
- the heat receiving part has a horizontally long rectangular parallelepiped shape with a front surface and a rear surface having a maximum area, a heat receiving plate, a heat dissipation internal path, a return internal path, a fin portion having a plurality of flat fins, an outlet, and an inlet And one or a plurality of partition walls, a plurality of heat receivers, a heat dissipation internal path opening, and a return internal path opening.
- the heat receiving plate is provided with a plurality of heating elements on at least one of the front surface and the rear surface.
- the heat dissipation internal path is provided in the upper part of the heat receiving part, and the refrigerant flows through the heat dissipation internal path.
- the return internal path is provided below the heat receiving part, and the refrigerant flows through the return internal path.
- the fin portion is provided between the heat dissipation internal path and the return internal path.
- the outflow port connects the heat dissipation path and the heat dissipation internal path.
- the inflow port connects the return path and the return internal path.
- the partition wall is provided between the front surface and the rear surface of the heat receiving unit so as to be parallel to the fins.
- the heat receiver is formed by being surrounded by the partition wall and the inner wall of the heat receiving portion.
- the heat radiation internal path opening communicates the heat radiation internal path of each heat receiver in the partition wall.
- the return internal path opening communicates the return internal path of each heat receiver in the partition wall.
- the inflow port and the outflow port are provided on the same side surface of the heat receiving unit.
- the fin portion protrudes inward from the heat receiving plate, and is provided so that the refrigerant flow path constituted by the gap between the fins is in the vertical direction.
- the calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is smaller than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate. In this way, the liquid-phase refrigerant spreads to the most downstream heat receiver on the return path side. Thereby, the dry-out of the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
- the liquid-phase refrigerant in the return path flows into the return internal path from the inflow port, and flows out from the return internal path to the fin portion. Then, the liquid-phase refrigerant that has flowed out to the fin portion receives heat generated from the heating element via the fins, becomes a two-phase refrigerant of a gas phase and a liquid phase, and is in a high pressure state. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
- the heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is configured to be smaller than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate. Therefore, the temperature of the most downstream heat receiver is lower than the temperature of the upstream heat receiver. Therefore, in the most downstream heat receiver, since the amount of heat received by the refrigerant is smaller than that of the upstream heat receiver, the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant is also small. Accordingly, the pressure in the most downstream heat receiver is lower than the pressure in the upstream heat receiver. Thereby, a refrigerant
- the heating value of the heating element installed on the most downstream heat receiving plate on the return path side is configured to be smaller than the heating value of the heating element installed upstream. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
- the heat receiving unit may include a partition plate provided between the return internal path and the fin portion so as to be parallel to the bottom surface of the heat receiving unit, and the partition plate may have a plurality of openings. .
- the partition plate provided between the return internal path and the fin portion has a plurality of openings, the liquid-phase refrigerant in the return path flows into the return internal path from the inlet and is provided in the partition plate. It flows out from the opening into the heat receiving part.
- the liquid phase refrigerant is supplied to the fin portion only from the opening of the partition plate, a large amount of the liquid phase refrigerant is prevented from flowing out from the return internal path to the fin portion. Thereby, dryout is suppressed in the downstream heat receiver.
- the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
- the heat receiving section is provided in a return internal path and includes a return internal pipe through which the refrigerant flows, and the return internal path opening communicates with the return internal pipe of each heat receiver in the partition wall. May be configured to have a plurality of openings.
- the liquid-phase refrigerant in the return path flows into the return internal pipe from the inflow port, and flows out into the heat receiving section from the opening provided in the return internal pipe. To do. Then, the liquid-phase refrigerant that has flowed out to the fin portion receives heat generated from the heating element via the fins, becomes a two-phase refrigerant of a gas phase and a liquid phase, and is in a high pressure state. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
- the heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is configured to be smaller than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate. Therefore, the temperature of the most downstream heat receiver is lower than the temperature of the upstream heat receiver. Therefore, in the most downstream heat receiver, since the amount of heat received by the refrigerant is smaller than that of the upstream heat receiver, the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant is also small. Accordingly, the pressure in the most downstream heat receiver is lower than the pressure in the upstream heat receiver. The refrigerant easily flows to the downstream most downstream heat receiver. Therefore, dryout is suppressed in the most downstream heat receiver on the return path side.
- the cooling device having the above-described configuration can suppress the liquid-phase refrigerant from being vaporized in the return internal pipe and preventing the vaporized refrigerant from flowing backward to the return path.
- the heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is larger than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate.
- the structure is also small. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
- the total opening area of the opening portions of the partition plates in each heat receiver may be the smallest in the most upstream heat receiver, and may be configured to increase as the downstream heat receiver becomes.
- the partition plate provided between the return internal path and the fin portion has a plurality of openings, the liquid phase refrigerant in the return path flows into the return internal path from the inflow port, and the opening provided in the partition plate Out into the heat receiving part.
- the total opening area of the openings of the partition plates in each heat receiver is configured to be the smallest in the most upstream heat receiver and increase as the downstream heat receiver is reached. Therefore, since the total opening area is small in the most upstream heat receiver, the liquid-phase refrigerant hardly flows out from the opening of the partition plate in the most upstream heat receiver. In addition, since the total opening area increases as the downstream heat receiver becomes, the liquid phase refrigerant tends to flow out from the opening of the partition plate as the downstream heat receiver becomes. Thereby, dryout is suppressed in the downstream heat receiver.
- the total opening area of the opening portions of the partition plates in each heat receiver may be the smallest in the most upstream heat receiver and may increase as the downstream heat receiver is increased. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
- the total opening area of the opening of the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the downstream heat receiver becomes larger.
- the liquid-phase refrigerant in the return route flows into the return internal conduit from the inlet and flows out into the heat receiving portion from the opening provided in the return internal conduit.
- the total opening area of the opening of the return internal pipe line in each heat receiver is configured to be the smallest in the most upstream heat receiver and increase as it becomes the downstream heat receiver. Therefore, since the total opening area is small in the most upstream heat receiver, the liquid-phase refrigerant hardly flows out from the opening of the return internal pipe line in the most upstream heat receiver. Further, since the total opening area becomes larger as the downstream heat receiver becomes, the liquid-phase refrigerant tends to flow out from the opening of the return internal pipe line as the downstream heat receiver becomes. Thereby, dryout is suppressed in the downstream heat receiver.
- the total opening area of the opening portion of the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver and may be increased as the downstream heat receiver is reached. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
- the number of openings of the partition plate in each heat receiver may be the smallest in the most upstream heat receiver and may be increased as the downstream heat receiver is reached.
- the liquid-phase refrigerant hardly flows out from the opening of the partition plate in the most upstream heat receiver.
- the number of openings of the partition plate increases as the downstream heat receiver becomes, the liquid phase refrigerant tends to flow out from the opening of the partition plate as the downstream heat receiver becomes. Thereby, dryout is suppressed in the downstream heat receiver.
- the number of openings of the partition plate in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the number of downstream heat receivers increases. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
- the number of openings of the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the number of downstream heat receivers increases.
- the number of openings in the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the number of downstream heat receivers increases. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
- the heating element may be installed on the heat receiving plate at a distance from the bottom surface of the heat receiving unit.
- the heating element is configured to be installed on the heat receiving plate at a distance from the bottom surface of the heat receiving part, so that the liquid phase refrigerant flowing in the return internal path provided at the lower part of the heat receiving part, that is, the heat receiving part
- the liquid refrigerant flowing through the bottom surface is spaced from the heating element. Therefore, the liquid phase refrigerant is less likely to receive heat from the heating element. Therefore, the liquid-phase refrigerant flowing in the return internal path receives heat and becomes a gas-phase refrigerant, and a state where the liquid-phase refrigerant does not reach the downstream of the return internal path through the fin portion is suppressed. Thereby, dryout is suppressed downstream of the heat receiving part on the return path side.
- the heating element may be installed on the heat receiving plate at a distance from the bottom surface of the heat receiving unit. Thereby, the dry-out downstream of the heat receiving part on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
- the electronic apparatus according to an embodiment of the present invention may be equipped with the cooling device having the above-described configuration.
- the electronic device having the above-described configuration can operate stably because it is equipped with a cooling device having high cooling performance.
- FIG. 1 is a schematic diagram of an electronic device equipped with the cooling device of the first embodiment.
- the electronic device 50 has a first heating element group 28, a second heating element group 29, and a cooling device 1 mounted in a case 51.
- the first heating element group 28 and the second heating element group 29 are composed of a plurality of heating elements.
- the first heating element group 28 and the second heating element group 29 include, for example, a power semiconductor element, a central processing unit (CPU), a large scale integrated circuit (LSI), an insulated gate bipolar transistor (IGBT), a diode, and the like.
- the heating element may be configured.
- the cooling device 1 cools the first heating element group 28 and the second heating element group 29 by the phase change of the refrigerant.
- the cooling device 1 includes a refrigerant circulation path formed by sequentially connecting the heat receiving section 3, the heat radiation path 5, the heat radiation section 4, and the return path 6. With this configuration, the inside of the circulation path provided in the cooling device 1 is a sealed space. Although not shown in FIG. 1, the refrigerant is sealed in the circulation path after the pressure is reduced.
- chlorofluorocarbons, fluorinated solvents and the like are used, but are not limited thereto.
- Aluminum is suitable for the material of the heat receiving part 3, the heat radiating part 4, and the first fin 22 and the second fin 23, which will be described later, but is not limited thereto.
- the cooling device 1 is connected to a water cooling chiller (not shown) for cooling the refrigerant vaporized by the heat of the first heating element group 28 and the second heating element group 29.
- the cooling water cooled by the water cooling chiller is supplied from the cooling water supply path 7 to the heat radiating unit 4.
- the vaporized refrigerant is cooled and liquefied by exchanging heat with the cooling water of the water-cooled chiller in the heat radiating section 4.
- the heat-exchanged cooling water returns to the water-cooled chiller via the cooling water return path 8 and is cooled in the water-cooled chiller.
- the cooling method of the refrigerant is a water cooling method using a water cooling chiller, but an air cooling method using a cooling fan or other methods may be used.
- the circulation path provided in the cooling device 1 is one in which a refrigerant is sealed after the inside is depressurized.
- the pressure in the circulation path becomes the saturation pressure of the refrigerant according to the external temperature by the action of the refrigerant.
- the heat of the first heating element group 28 and the second heating element group 29 is transmitted to the refrigerant through the heat receiving portion 3, and the liquid refrigerant is vaporized, whereby the first heating element group 28 and the second heating element group 28 are heated.
- the body group 29 is cooled.
- the refrigerant vaporized in the heat receiving part 3 becomes a gas-liquid two-phase mixed flow with the liquid refrigerant not vaporized, and moves from the heat receiving part 3 to the heat radiating part 4 through the heat radiation path 5.
- the vaporized refrigerant is cooled by the cooling water of the water-cooled chiller supplied from the cooling water supply path 7, becomes a liquid-phase refrigerant again, and returns to the heat receiving unit 3 through the return path 6.
- the liquid-phase refrigerant is vaporized in the heat receiving part 3, the vaporized refrigerant passes through the heat radiation path 5 and is cooled and liquefied in the heat radiation part 4, and the liquefied refrigerant passes through the feedback path 6 and again.
- the cycle supplied into the heat receiving unit 3 is repeated.
- the cooling device 1 cools the first heating element group 28 and the second heating element group 29.
- the diameter of the return path 6 is smaller than the diameter of the heat dissipation path 5.
- FIG. 2 is a diagram illustrating an appearance of the heat receiving unit 3 of the cooling device 1 according to the first embodiment.
- FIG. 3 and 4 are exploded perspective views of the heat receiving unit 3 of the cooling device 1 according to the first embodiment.
- FIG. 5 is a view of the first heat receiving plate 15 of the heat receiving unit 3 of the cooling device according to the first embodiment as viewed from the front side.
- the heat receiving part 3 has a horizontally long rectangular parallelepiped shape with the maximum area on the front and rear surfaces.
- the heat receiving unit 3 is installed so that the front surface and the rear surface are parallel to the vertical direction.
- the heat receiving unit 3 includes a first heat receiving plate 15 on the front surface and a second heat receiving plate 16 on the rear surface.
- the first heat receiving plate 15 is provided with a first heating element group 28 (see FIG. 1)
- the second heat receiving plate 16 is provided with a second heating element group 29 (see FIG. 1).
- a heat generating body, a heat receiving plate, a fin, etc. are each divided into the first and second, this means that there are two each, and unless otherwise specified, the first and second There is no difference.
- the heat receiving section 3 includes two heating element groups and two heat receiving plates, respectively, but the first heating element group 28 is provided on either the front surface or the rear surface. Only the heat receiving plate 15 may be provided (not shown).
- the second heating element group 29 is composed of a first heating element 43, a second heating element 44, and a third heating element 45. Each heating element constituting the second heating element group 29 is brought into contact with the second heat receiving plate 16 to thermally connect each heating element and the second heat receiving plate 16.
- the first heating element group 28 is also composed of a plurality of heating elements. Each heating element constituting the first heating element group 28 is brought into contact with the first heat receiving plate 15 to thermally connect each heating element and the first heat receiving plate 15.
- the first heat receiving plate 15 and the second heat receiving plate 16 are appropriately provided with fixing screw holes 19 for fixing the heating element groups.
- first heat generating group 28 can be fixed to the first heat receiving plate 15 and the second heat generating group 29 can be fixed to the second heat receiving plate 16 with screws.
- the first heating element group 28 and the second heating element group 29 are installed so as to be parallel to the vertical direction so that the heat receiving portion 3 is sandwiched therebetween.
- a space is provided as a heat radiating internal path 25 at the top of the heat receiving portion 3 having a horizontally long rectangular parallelepiped shape.
- a space is provided as a return internal path 24 below the heat receiving unit 3. That is, the heat receiving unit 3 includes a heat dissipation internal path 25 and a return internal path 24. The refrigerant flows through the heat dissipation internal path 25 and the return internal path 24.
- the heat receiving portion 3 includes a fin portion 2 provided at a central portion between the heat dissipation internal path 25 and the return internal path 24.
- the heat receiving unit 3 includes an outlet 31 that connects the heat dissipation path 5 and the heat dissipation internal path 25, and an inlet 30 that connects the return path 6 and the return internal path 24.
- the outlet 31 and the inlet 30 are provided on the same side surface of the heat receiving unit 3.
- the side surface on which the outflow port 31 and the inflow port 30 are provided is a side surface that connects the front surface and the rear surface on which the first heat receiving plate 15 and the second heat receiving plate 16 are provided.
- the fin part 2 has a plurality of flat first fins 22 and a plurality of flat second fins 23.
- the first fin 22 protrudes from the first heat receiving plate 15 to the inside of the heat receiving portion 3, and is provided so that the refrigerant flow path constituted by the gap between the first fins 22 is in the vertical direction.
- the second fin 23 protrudes from the second heat receiving plate 16 to the inside of the heat receiving portion 3, and is provided so that the refrigerant flow path constituted by the gap between the second fins 23 is in the vertical direction.
- the heat receiving unit 3 includes a partition plate 32 provided between the return internal path 24 and the fin portion 2 so as to be parallel to the bottom surface of the heat receiving unit 3.
- the partition plate 32 has a plurality of openings 33.
- the heat receiving unit 3 is parallel to the first fin 22 and the second fin 23 between the front surface and the rear surface of the heat receiving unit 3, that is, between the first heat receiving plate 15 and the second heat receiving plate 16.
- One or a plurality of partition walls 34 are provided so as to be oriented.
- the heat receiving unit 3 includes two partition walls 34.
- the partition wall 34 is provided so as to divide the longitudinal direction of the heat receiving unit 3 into approximately equal parts.
- the heat receiving unit 3 includes a plurality of heat receivers 11 that are sections formed by being surrounded by the partition wall 34 and the inner wall of the heat receiving unit 3. In the present embodiment, three heat receivers 11 are formed.
- the heat receiving unit 3 includes a heat radiating internal path opening 35 that communicates the heat radiating internal path 25 of each heat receiver 11 in the partition wall 34. Further, the heat receiving unit 3 includes a return internal path opening 36 that communicates the return internal path 24 of each heat receiver 11 in the partition wall 34.
- the heat dissipating internal path opening 35 and the return internal path opening 36 may be openings actually provided in the partition wall 34, or the structure in which the partition wall 34 is provided avoiding the heat dissipating internal path 25 and the return internal path 24. It may be what you did.
- the partition plate 32 has a plurality of openings 33. At least one opening 33 is provided in one heat receiver 11.
- the pressure is low due to the action of the heat radiating unit 4 connected to the outlet 31. Therefore, the refrigerant that has flowed out into the fin portion 2 in the heat receiving portion 3 tends to flow to the side surface where the inlet 30 and the outlet 31 having a low pressure are installed.
- the lateral width of the heat receiving unit 3 may be increased. In such a case, the distance from the side surface where the inflow port 30 and the outflow port 31 are installed to the opposite side surface becomes longer.
- the refrigerant supplied to the heat receiver 11 that is a partitioned section flows through the first fin 22 and the second fin 23 in the heat receiver 11. .
- the refrigerant flows to the heat dissipation path 5 side through the heat dissipation internal path 25 and the heat dissipation internal path opening 35 provided in the partition wall 34. Therefore, even when the lateral width of the heat receiving part 3 is large, by partitioning the heat receiving part 3 with the partition wall 34, dryout in a region far from the side surface where the inlet 30 and the outlet 31 are installed is suppressed.
- the second heat receiving plate 16 is provided with a second heating element group 29 including a first heating element 43, a second heating element 44, and a third heating element 45. ing.
- the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiver 11 (the most upstream heat receiver 20.
- the amount of heat generated by each of the first heating element 43 and the second heating element 44 installed via the second heat receiving plate 16 is smaller.
- the amount of heat generated by the third heating element 45 installed on the most downstream side of the refrigerant flow viewed from the return path 6 side is the first installed on the upstream side of the most downstream side. It is smaller than each calorific value of the heating element 43 and the second heating element 44.
- upstream means the side closer to the return path 6, and downstream means the side far from the return path 6. That is, the most upstream heat receiver 20 is a heat receiver closest to the return path 6 among the heat receivers 11. The most downstream heat receiver 21 is a heat receiver farthest from the return path 6 among the heat receivers 11.
- the partition plate 32 provided between the return internal path 24 and the fin portion 2 so as to be parallel to the bottom surface of the heat receiving portion 3 has a plurality of openings 33. Therefore, the liquid-phase refrigerant in the return path 6 flows into the return internal path 24 from the inflow port 30, and flows out from the opening 33 provided in the partition plate 32 to the fin portion 2. Then, the liquid-phase refrigerant that has flowed out to the fin portion 2 receives heat generated from the first heating element 43 installed on the upstream side via the second fin 23, and the two phases of the gas phase and the liquid phase are received. It becomes a refrigerant of the phase, and the pressure becomes high. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
- the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is the upstream heat receiver 11 (including the most upstream heat receiver 20).
- the first heat generating body 43 and the second heat generating body 44 installed through the second heat receiving plate 16 are configured to have a smaller heat generation amount. Therefore, the temperature of the most downstream heat receiver 21 is lower than the temperature of the upstream heat receiver 11 (including the most upstream heat receiver 20). Therefore, in the most downstream heat receiver 21, since the amount of heat received by the refrigerant is less than that of the upstream heat receiver 11 (including the most upstream heat receiver 20), the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant. There are few.
- the pressure in the most downstream heat receiver 21 is lower than the pressure in the upstream heat receiver 11 (including the most upstream heat receiver 20).
- the refrigerant easily flows to the most downstream heat receiver 21 having a low pressure. Therefore, dryout is suppressed in the most downstream heat receiver 21 on the return path 6 side.
- the amount of heat generated by the third heating element 45 installed in the most downstream heat receiving device 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiving device 11 (the most upstream heat receiving device 11).
- the heat generation amount of each of the first heat generating body 43 and the second heat generating body 44 installed in the heat receiving device 20 via the second heat receiving plate 16 is smaller. Thereby, the dry-out in the most downstream heat receiver 21 is suppressed. That is, the cooling device 1 does not need to fill the heat receiving unit 3 with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving unit 3, and has high cooling performance. .
- the total opening area of the openings 33 of the partition plate 32 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may be configured to increase as the downstream heat receiver 11 is reached.
- the total opening area means the total area of the openings of the opening 33 in each heat receiver 11.
- the partition plate 32 has a plurality of openings 33.
- the liquid-phase refrigerant cooled and liquefied by the heat radiating unit 4 flows through the return path 6 and flows into the return internal path 24 from the inlet 30 of the most upstream heat receiving unit 3 on the return path 6 side.
- the liquid refrigerant flowing into the return internal path 24 receives the heat generated from the first heating element group 28 and the second heating element group 29 via the heat receiving unit 3, and the gas phase, the liquid phase, And the pressure is high. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
- This high-pressure two-phase refrigerant flows out from the plurality of openings 33 of the partition plate 32 to the fin portion 2, flows upward in the vertical gaps of the first fin 22 and the second fin 23, Liquid phase refrigerant is supplied to the surfaces of the first fin 22 and the second fin 23. Then, while receiving heat from the first fin 22 and the second fin 23, the refrigerant flows into the outlet 31 having a low pressure through the heat radiation internal path 25 by the action of the heat radiation unit 4.
- the liquid-phase refrigerant is not supplied from the return path 6, but from one upstream heat receiver 11. Supplied. That is, the liquid-phase refrigerant in the heat receiver 11 that is one upstream is supplied to the heat receiver 11 from the return internal path opening 36 provided in the partition wall 34. The subsequent operation is the same as that in the most upstream heat receiver 20.
- the total opening area of the openings 33 of the partition plate 32 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and increase as the downstream heat receiver 11 is reached. Therefore, since the total opening area is small in the most upstream heat receiver 20, the liquid-phase refrigerant hardly flows out from the opening 33 of the partition plate 32 in the most upstream heat receiver 20. Further, since the total opening area becomes larger as the downstream heat receiver 11 is reached, the liquid phase refrigerant is more likely to flow out from the opening 33 of the partition plate 32 as the downstream heat receiver 11 is reached. Thereby, in the downstream heat receiver 11, dryout is suppressed.
- the total opening area of the openings 33 of the partition plate 32 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and become larger toward the downstream heat receiver 11. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed.
- the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
- the number of openings 33 of the partition plate 32 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may increase as the number of downstream heat receivers 11 increases.
- the number of openings 33 of the partition plate 32 in the most upstream heat receiver 20 is the smallest, the liquid-phase refrigerant hardly flows out from the openings 33 of the partition plate 32 in the most upstream heat receiver 20.
- the number of the openings 33 increases as the downstream heat receiver 11 is reached, the liquid-phase refrigerant is more likely to flow out from the openings 33 of the partition plate 32 as the downstream heat receiver 11 is reached. Thereby, in the downstream heat receiver 11, dryout is suppressed.
- the number of the openings 33 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may be increased as the downstream heat receiver 11 is reached. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed.
- the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
- the first heating element group 28 and the second heating element group 29 are spaced apart from the bottom surface of the heat receiving unit 3 by the first heat receiving plate 15 and the second heat receiving plate 16, respectively. You may make it the structure installed in.
- the liquid-phase refrigerant flowing in the return internal path 24 provided in the lower part of the heat receiving unit 3, that is, the liquid-phase refrigerant flowing in the bottom surface of the heat receiving unit 3, the first heating element group 28 and the second The distance from the heating element group 29 is set. Therefore, the refrigerant hardly receives heat from the first heating element group 28 and the second heating element group 29. Therefore, the liquid-phase refrigerant flowing in the return internal path 24 receives heat and becomes a gas-phase refrigerant, and the state where the liquid-phase refrigerant flows out to the fin portion 2 and does not reach the downstream of the return internal path 24 is suppressed. Thereby, dryout is suppressed downstream of the heat receiving part 3 on the return path 6 side.
- the first heating element group 28 and the second heating element group 29 are separated from the bottom surface of the heat receiving unit 3 by the first heat receiving plate 15 and the second heat receiving plate 16, respectively. It may be configured to be installed. Thereby, the dryout of the downstream of the heat receiving part 3 by the side of the return path 6 is suppressed. That is, the cooling device 1 does not need to fill the heat receiving unit 3 with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving unit 3, and has high cooling performance. .
- FIG. 6 is an exploded perspective view of the heat receiving unit 3 of the cooling device 1 according to the second embodiment.
- FIG. 7 is a view of the first heat receiving plate 15 of the heat receiving unit 3 of the cooling device 1 according to the second embodiment as viewed from the front side.
- the heat receiving unit 3 includes a return internal pipe 37 connected to the inflow port 30.
- the return internal pipe 37 is provided in the return internal path 24, and the refrigerant flows through the return internal pipe 37.
- the inflow port 30 connects the return path 6 and the return internal conduit 37.
- the return internal path opening 36 communicates the return internal pipe line 37 of each heat receiver 11 in the partition wall 34.
- the return internal conduit 37 has a plurality of openings 38.
- the heat receiving unit 3 is parallel to the first fin 22 and the second fin 23 between the front surface and the rear surface of the heat receiving unit 3, that is, between the first heat receiving plate 15 and the second heat receiving plate 16.
- One or a plurality of partition walls 34 are provided so as to be oriented.
- the heat receiving unit 3 includes two partition walls 34.
- the partition wall 34 is provided so as to divide the longitudinal direction of the heat receiving unit 3 into approximately equal parts.
- the heat receiving unit 3 includes a plurality of heat receivers 11 that are sections formed by being surrounded by the partition wall 34 and the inner wall of the heat receiving unit 3. In the present embodiment, three heat receivers 11 are formed.
- the heat receiving unit 3 includes a heat radiating internal path opening 35 that communicates with the heat radiating internal path 25 of each of the heat receivers 11 at the upper part of the heat receiving unit 3 in the partition wall 34.
- the heat receiving unit 3 includes a return internal path opening 36 in the partition wall 34, which is located below the heat receiving unit 3 and communicates with the return internal pipe line 37 of each heat receiver 11.
- the heat dissipating internal path opening 35 and the return internal path opening 36 may be openings actually provided in the partition wall 34, or the structure in which the partition wall 34 is provided avoiding the heat dissipating internal path 25 and the return internal conduit 37. It may be what.
- the return internal conduit 37 has a plurality of openings 38. At least one opening 38 is provided in one heat receiver 11.
- the second heat receiving plate 16 is provided with a second heating element group 29 including a first heating element 43, a second heating element 44, and a third heating element 45. ing.
- the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiver 11 (the most upstream heat receiver 20.
- the amount of heat generated by each of the first heat generating body 43 and the second heat generating body 44 installed via the first heat receiving plate 15 is smaller.
- the amount of heat generated by the third heating element 45 installed on the most downstream side of the refrigerant flow viewed from the return path 6 side is the first installed on the upstream side of the most downstream side. It is smaller than each calorific value of the heating element 43 and the second heating element 44.
- the liquid-phase refrigerant in the return path 6 flows into the return internal pipe 37 from the inlet 30 and is provided in the return internal pipe 37. It flows out from 38 to the fin part 2. Then, the liquid-phase refrigerant that has flowed out to the fin portion 2 receives heat generated from the first heating element 43 installed on the upstream side via the second fin 23, and the two phases of the gas phase and the liquid phase are received. It becomes a refrigerant of the phase, and the pressure becomes high. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
- the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is the upstream heat receiver 11 (including the most upstream heat receiver 20).
- the first heat generating body 43 and the second heat generating body 44 installed through the second heat receiving plate 16 are configured to have a smaller heat generation amount. Therefore, the temperature of the most downstream heat receiver 21 is lower than the temperature of the upstream heat receiver 11 (including the most upstream heat receiver 20). Therefore, in the most downstream heat receiver 21, since the amount of heat received by the refrigerant is less than that of the upstream heat receiver 11 (including the most upstream heat receiver 20), the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant. There are few.
- the pressure in the most downstream heat receiver 21 is lower than the pressure in the upstream heat receiver 11 (including the most upstream heat receiver 20).
- the refrigerant easily flows to the most downstream heat receiver 21 having a low pressure. Therefore, dryout is suppressed in the most downstream heat receiver 21 on the return path 6 side.
- the cooling device 1 can prevent the liquid-phase refrigerant from evaporating in the return internal pipe 37 and flowing back to the return path 6 side.
- the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiver 11 (the most upstream heat receiver 11).
- the first heat generating body 43 and the second heat generating body 44 installed in the heat receiving device 20 via the second heat receiving plate 16 are configured to have a smaller heat generation amount. Thereby, the dry-out in the most downstream heat receiver 21 is suppressed. That is, the cooling device 1 does not need to fill the heat receiving unit 3 with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving unit 3, and has high cooling performance. .
- the total opening area of the opening portions 38 of the return internal pipes 37 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may be increased as the downstream heat receiver 11 is reached.
- the return internal conduit 37 has a plurality of openings 38.
- the liquid-phase refrigerant cooled and liquefied by the heat radiating unit 4 flows through the return path 6 and flows into the return internal conduit 37 from the inlet 30 of the most upstream heat receiving unit 3 on the return path 6 side.
- the liquid refrigerant flowing into the return internal pipe 37 receives the heat generated from the first heating element group 28 and the second heating element group 29 via the heat receiving unit 3, and the gas phase and the liquid phase are received. And the pressure is high. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
- the high-pressure two-phase refrigerant flows out from the plurality of openings 38 of the return internal pipe 37 to the fin portion 2 and flows upward through the vertical gaps of the first fin 22 and the second fin 23.
- the liquid-phase refrigerant is supplied to the surfaces of the first fin 22 and the second fin 23.
- the refrigerant flows into the outlet 31 having a low pressure through the heat radiation internal path 25 by the action of the heat radiation unit 4.
- the liquid-phase refrigerant is not supplied from the return path 6, but from one upstream heat receiver 11. Supplied. That is, the liquid-phase refrigerant in the return internal conduit 37 in the upstream heat receiver 11 passes through the return internal passage opening 36 provided in the partition wall 34 to the return internal conduit 37 in the downstream heat receiver 11. Supplied. The subsequent operation is the same as that in the most upstream heat receiver 20.
- the total opening area of the openings 38 of the return internal pipes 37 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and increase as the downstream heat receiver 11 is reached. Therefore, since the total opening area of the most upstream heat receiver 20 is small, the liquid phase refrigerant hardly flows out from the opening 38 of the return internal pipe 37 in the most upstream heat receiver 20. Further, since the total opening area becomes larger as the downstream heat receiver 11 is reached, the liquid phase refrigerant is more likely to flow out from the opening 38 of the return internal pipe 37 as the downstream heat receiver 11 is reached. Thereby, in the downstream heat receiver 11, dryout is suppressed.
- the total opening area of the openings 38 of the return internal pipe 37 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and increase as the downstream heat receiver 11 is reached. Yes. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed. In other words, the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
- the number of openings 38 of the return internal pipe 37 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may increase as the downstream heat receiver 11 is reached.
- the number of openings 38 of the return internal conduit 37 in the most upstream heat receiver 20 is the smallest, so that the liquid-phase refrigerant flows out from the opening 38 of the return internal conduit 37 in the most upstream heat receiver 20. Hateful.
- the number of the opening portions 38 increases as the downstream heat receiver 11 is reached, the liquid phase refrigerant is more likely to flow out from the opening portion 38 of the return internal pipe 37 as the downstream heat receiver 11 is formed. Thereby, in the downstream heat receiver 11, dryout is suppressed.
- the number of openings 38 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may increase as the number of downstream heat receivers 11 increases. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed. In other words, the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
- the cooling device since the cooling device according to the present invention has high cooling performance, it cools electronic components such as a central processing unit (CPU), a large scale integrated circuit (LSI), an insulated gate bipolar transistor (IGBT), and a diode. It is useful as a cooling device.
- CPU central processing unit
- LSI large scale integrated circuit
- IGBT insulated gate bipolar transistor
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Abstract
In the present invention, a heat receiving part (3) has an oblong rectangular parallelepiped shape in which a front face and a rear face have the largest surface area, the heat receiving part comprising: a heat receiving plate; a heat radiation internal path (25); a feedback internal path (24); a fin part (2) having a plurality of flat plate-shaped fins; an outlet (31); an inlet (30); one or a plurality of partition walls (34); a plurality of heat receivers (11); a heat radiation internal path opening (35); and a feedback internal path opening (36). In the heat receiving plate, a plurality of heating elements are disposed on the front face and/or the rear face. The partition walls (34) are provided between the front face and the rear face of the heat receiving part (3) and are oriented in a direction parallel to the fins. The heat receivers (11) are formed to be surrounded by the partition walls (34) and the inner walls of the heat receiving part (3). The amount of heat generated by the heating elements disposed via the heat receiving plate to the most downstream heat receiver (21) on the feedback path (6) side is less than the amount of heat generated by the heating elements disposed via the heat receiving plate to the upstream heat receivers.
Description
本発明は、電子部品を冷却する冷却装置およびこれを搭載した電子機器に関する。
The present invention relates to a cooling device for cooling an electronic component and an electronic apparatus equipped with the cooling device.
従来から、この種の冷却装置として、以下のような構成が知られている。
Conventionally, the following configuration is known as this type of cooling device.
すなわち、図8に示すように、従来の冷却装置110は、受熱部である筐体112を備え、筐体112は、冷媒が流入する流入口114と、冷媒が流出する流出口116と、管路部130とを備える。管路部130には、蒸発器部132と流通部134とが隣接して設けられている。蒸発器部132において、流入口114から流入した冷媒が発熱体であるインバータ108の熱によって気化する。気化した冷媒は、流通部134を流通して、流出口116から流出する。蒸発器部132には、底壁部120から流通部134の側に向かって突出する複数のフィン140が設けられている。冷媒は、複数のフィン140の間の隙間を流通する(例えば特許文献1参照)。
That is, as shown in FIG. 8, a conventional cooling device 110 includes a housing 112 that is a heat receiving portion, and the housing 112 includes an inlet 114 through which a refrigerant flows, an outlet 116 through which a refrigerant flows, and a pipe. And a road portion 130. In the pipe line section 130, an evaporator section 132 and a circulation section 134 are provided adjacent to each other. In the evaporator section 132, the refrigerant flowing from the inlet 114 is vaporized by the heat of the inverter 108, which is a heating element. The vaporized refrigerant flows through the flow part 134 and flows out from the outlet 116. The evaporator part 132 is provided with a plurality of fins 140 that protrude from the bottom wall part 120 toward the flow part 134. A refrigerant | coolant distribute | circulates the clearance gap between the some fin 140 (for example, refer patent document 1).
特許文献1に示される従来の冷却装置110において、インバータ108は筐体112の底面に水平に設置されているため、筐体112の底壁部120は液相の冷媒で満たされている。冷媒は、底壁部120から流通部134の側に向かって突出した複数のフィン140の間の隙間を流通する。
In the conventional cooling device 110 disclosed in Patent Document 1, since the inverter 108 is installed horizontally on the bottom surface of the housing 112, the bottom wall portion 120 of the housing 112 is filled with a liquid-phase refrigerant. The refrigerant flows through the gaps between the plurality of fins 140 protruding from the bottom wall part 120 toward the flow part 134.
このような構成の筐体112の流入口114から流出口116までの距離を長くして、複数のインバータ108を冷却することが行われている。このような場合には、流入口114から近い範囲、すなわち筐体112の上流において多くの液相の冷媒が気化し、筐体112の下流において液相の冷媒が充分に行き渡らないと、冷却装置110はインバータ108を冷却することができない状態になる。この状態が、いわゆるドライアウトの状態である。この状態では、インバータ108の温度が上昇してしまう。かといって、ドライアウトを抑制するために、過剰な量の液相の冷媒を供給すると、厚い液相の冷媒の層がフィン140を覆い、熱抵抗となる。そうすると、冷却装置110は、薄い液相の冷媒の層がフィン140を覆う理想的な状態を作り出すことができず、冷却装置110の冷却性能が低くなる。
The plurality of inverters 108 are cooled by increasing the distance from the inlet 114 to the outlet 116 of the casing 112 having such a configuration. In such a case, if a large amount of liquid-phase refrigerant is vaporized in a range close to the inlet 114, that is, upstream of the casing 112, and the liquid-phase refrigerant does not spread sufficiently downstream of the casing 112, the cooling device 110 becomes a state where the inverter 108 cannot be cooled. This state is a so-called dry-out state. In this state, the temperature of the inverter 108 increases. However, if an excessive amount of liquid-phase refrigerant is supplied in order to suppress dry-out, a thick liquid-phase refrigerant layer covers the fins 140 and becomes thermal resistance. Then, the cooling device 110 cannot create an ideal state in which a thin liquid phase refrigerant layer covers the fins 140, and the cooling performance of the cooling device 110 is lowered.
そこで、本発明に係る冷却装置は、受熱部の帰還経路側の最下流まで液相の冷媒が行き渡る構成としている。これにより、受熱部の帰還経路側の下流のドライアウトが抑制される。すなわち、本発明に係る冷却装置は、過剰な量の液相の冷媒で受熱部内を満たす必要が無く、薄い液相の冷媒の層を受熱部内に形成することができ、高い冷却性能を有する。
Therefore, the cooling device according to the present invention is configured such that the liquid phase refrigerant reaches the most downstream side on the return path side of the heat receiving portion. Thereby, the downstream dryout of the heat receiving part on the return path side is suppressed. That is, the cooling device according to the present invention does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
そして、この目的を達成するために、本発明に係る冷却装置は、冷媒の相変化によって発熱体を冷却する冷却装置であって、受熱部、放熱経路、放熱部および帰還経路を順に連結して形成される冷媒の循環経路を備える。受熱部は、前面および後面が最大面積の横長の直方体形状であり、受熱板と、放熱内部経路と、帰還内部経路と、複数の平板状のフィンを有するフィン部と、流出口と、流入口と、1または複数の仕切壁と、複数の受熱器と、放熱内部経路開口と、帰還内部経路開口とを備える。受熱板は、前面または後面の少なくとも一方に複数の発熱体が設置される。放熱内部経路は受熱部の上部に設けられ、冷媒が放熱内部経路を流通する。帰還内部経路は受熱部の下部に設けられ、冷媒が帰還内部経路を流通する。フィン部は、放熱内部経路と帰還内部経路との間に設けられる。流出口は、放熱経路と放熱内部経路とを接続する。流入口は、帰還経路と帰還内部経路とを接続する。仕切壁は、受熱部の前面と後面との間に、フィンと平行方向になるように設けられる。受熱器は、仕切壁と受熱部の内壁とで囲まれて形成される。放熱内部経路開口は、仕切壁において、各受熱器の放熱内部経路を連通させる。帰還内部経路開口は、仕切壁において、各受熱器の帰還内部経路を連通させる。流入口と流出口とは、受熱部の同一の側面に設けられる。フィン部は、受熱板から内部に突出し、フィン間の隙間により構成される冷媒の流路が上下方向となるように設けられる。帰還経路側の最下流の受熱器に受熱板を介して設置された発熱体の発熱量は、上流の受熱器に受熱板を介して設置された発熱体の発熱量よりも小さい。これにより、所期の目的を達成する。
In order to achieve this object, a cooling device according to the present invention is a cooling device that cools a heating element by a phase change of a refrigerant, and sequentially connects a heat receiving unit, a heat radiation path, a heat radiation unit, and a return path. A circulation path for the formed refrigerant is provided. The heat receiving part has a horizontally long rectangular parallelepiped shape with a front surface and a rear surface having a maximum area, a heat receiving plate, a heat dissipation internal path, a return internal path, a fin portion having a plurality of flat fins, an outlet, and an inlet And one or a plurality of partition walls, a plurality of heat receivers, a heat dissipation internal path opening, and a return internal path opening. The heat receiving plate is provided with a plurality of heating elements on at least one of the front surface and the rear surface. The heat dissipation internal path is provided in the upper part of the heat receiving part, and the refrigerant flows through the heat dissipation internal path. The return internal path is provided below the heat receiving part, and the refrigerant flows through the return internal path. The fin portion is provided between the heat dissipation internal path and the return internal path. The outflow port connects the heat dissipation path and the heat dissipation internal path. The inflow port connects the return path and the return internal path. The partition wall is provided between the front surface and the rear surface of the heat receiving unit so as to be parallel to the fins. The heat receiver is formed by being surrounded by the partition wall and the inner wall of the heat receiving portion. The heat radiation internal path opening communicates the heat radiation internal path of each heat receiver in the partition wall. The return internal path opening communicates the return internal path of each heat receiver in the partition wall. The inflow port and the outflow port are provided on the same side surface of the heat receiving unit. The fin portion protrudes inward from the heat receiving plate, and is provided so that the refrigerant flow path constituted by the gap between the fins is in the vertical direction. The calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is smaller than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate. This achieves the intended purpose.
以上のように、本発明に係る冷却装置は、冷媒の相変化によって発熱体を冷却する冷却装置であって、受熱部、放熱経路、放熱部および帰還経路を順に連結して形成される冷媒の循環経路を備える。受熱部は、前面および後面が最大面積の横長の直方体形状であり、受熱板と、放熱内部経路と、帰還内部経路と、複数の平板状のフィンを有するフィン部と、流出口と、流入口と、1または複数の仕切壁と、複数の受熱器と、放熱内部経路開口と、帰還内部経路開口とを備える。受熱板は、前面または後面の少なくとも一方に複数の発熱体が設置される。放熱内部経路は受熱部の上部に設けられ、冷媒が放熱内部経路を流通する。帰還内部経路は受熱部の下部に設けられ、冷媒が帰還内部経路を流通する。フィン部は、放熱内部経路と帰還内部経路との間に設けられる。流出口は、放熱経路と放熱内部経路とを接続する。流入口は、帰還経路と帰還内部経路とを接続する。仕切壁は、受熱部の前面と後面との間に、フィンと平行方向になるように設けられる。受熱器は、仕切壁と受熱部の内壁とで囲まれて形成される。放熱内部経路開口は、仕切壁において、各受熱器の放熱内部経路を連通させる。帰還内部経路開口は、仕切壁において、各受熱器の帰還内部経路を連通させる。流入口と流出口とは、受熱部の同一の側面に設けられる。フィン部は、受熱板から内部に突出し、フィン間の隙間により構成される冷媒の流路が上下方向となるように設けられる。帰還経路側の最下流の受熱器に受熱板を介して設置された発熱体の発熱量は、上流の受熱器に受熱板を介して設置された発熱体の発熱量よりも小さい。このようにして、受熱部の帰還経路側の最下流まで液相の冷媒が行き渡る構成としている。これにより、受熱部の帰還経路側の下流のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱部内を満たす必要が無く、薄い液相の冷媒の層を受熱部内に形成することができ、高い冷却性能を有する。
As described above, the cooling device according to the present invention is a cooling device that cools a heating element by a phase change of the refrigerant, and is a refrigerant that is formed by sequentially connecting a heat receiving part, a heat radiation path, a heat radiation part, and a return path. Provide a circulation path. The heat receiving part has a horizontally long rectangular parallelepiped shape with a front surface and a rear surface having a maximum area, a heat receiving plate, a heat dissipation internal path, a return internal path, a fin portion having a plurality of flat fins, an outlet, and an inlet And one or a plurality of partition walls, a plurality of heat receivers, a heat dissipation internal path opening, and a return internal path opening. The heat receiving plate is provided with a plurality of heating elements on at least one of the front surface and the rear surface. The heat dissipation internal path is provided in the upper part of the heat receiving part, and the refrigerant flows through the heat dissipation internal path. The return internal path is provided below the heat receiving part, and the refrigerant flows through the return internal path. The fin portion is provided between the heat dissipation internal path and the return internal path. The outflow port connects the heat dissipation path and the heat dissipation internal path. The inflow port connects the return path and the return internal path. The partition wall is provided between the front surface and the rear surface of the heat receiving unit so as to be parallel to the fins. The heat receiver is formed by being surrounded by the partition wall and the inner wall of the heat receiving portion. The heat radiation internal path opening communicates the heat radiation internal path of each heat receiver in the partition wall. The return internal path opening communicates the return internal path of each heat receiver in the partition wall. The inflow port and the outflow port are provided on the same side surface of the heat receiving unit. The fin portion protrudes inward from the heat receiving plate, and is provided so that the refrigerant flow path constituted by the gap between the fins is in the vertical direction. The calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is smaller than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate. In this way, the liquid-phase refrigerant spreads to the most downstream side on the return path side of the heat receiving portion. Thereby, the downstream dryout of the heat receiving part on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
すなわち、帰還経路の液相の冷媒は、流入口から帰還内部経路に流入し、帰還内部経路からフィン部に流出する。そして、フィン部に流出した液相の冷媒は、フィンを介して発熱体から発生した熱を受熱し、気相と液相との二相の冷媒となり、圧力が高い状態となる。これは、冷媒が気化するときに、冷媒の体積が膨張するためである。
That is, the liquid-phase refrigerant in the return path flows into the return internal path from the inflow port, and flows out from the return internal path to the fin portion. Then, the liquid-phase refrigerant that has flowed out to the fin portion receives heat generated from the heating element via the fins, becomes a two-phase refrigerant of a gas phase and a liquid phase, and is in a high pressure state. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
帰還経路側の最下流の受熱器に受熱板を介して設置された発熱体の発熱量は、上流の受熱器に受熱板を介して設置された発熱体の発熱量よりも小さい構成としている。そのため、最下流の受熱器の温度は、上流側の受熱器の温度より低温となる。そのため、最下流の受熱器においては、上流側の受熱器より冷媒が受熱する熱量が少ないため、液相の冷媒が気化して膨張する冷媒の体積も少ない。従って、最下流の受熱器内の圧力は、上流側の受熱器内の圧力より低くなる。冷媒は、圧力の低い最下流の受熱器に流れやすくなる。そのため、帰還経路側の下流の受熱器において、ドライアウトが抑制される。
The heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is configured to be smaller than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate. Therefore, the temperature of the most downstream heat receiver is lower than the temperature of the upstream heat receiver. Therefore, in the most downstream heat receiver, since the amount of heat received by the refrigerant is smaller than that of the upstream heat receiver, the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant is also small. Accordingly, the pressure in the most downstream heat receiver is lower than the pressure in the upstream heat receiver. The refrigerant easily flows to the downstream most downstream heat receiver. Therefore, dryout is suppressed in the downstream heat receiver on the return path side.
以上のようにして、帰還経路側の最下流の受熱器に受熱板を介して設置された発熱体の発熱量は、上流の受熱器に受熱板を介して設置された発熱体の発熱量よりも小さい構成としている。これにより、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は過剰な量の液相の冷媒で受熱部内を満たす必要が無く、薄い液相の冷媒の層を受熱部内に形成することができ、高い冷却性能を有する。
As described above, the calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is larger than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate. The structure is also small. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
本発明の一実施形態に係る冷却装置は、冷媒の相変化によって発熱体を冷却する冷却装置であって、受熱部、放熱経路、放熱部および帰還経路を順に連結して形成される冷媒の循環経路を備える。受熱部は、前面および後面が最大面積の横長の直方体形状であり、受熱板と、放熱内部経路と、帰還内部経路と、複数の平板状のフィンを有するフィン部と、流出口と、流入口と、1または複数の仕切壁と、複数の受熱器と、放熱内部経路開口と、帰還内部経路開口とを備える。受熱板は、前面または後面の少なくとも一方に複数の発熱体が設置される。放熱内部経路は受熱部の上部に設けられ、冷媒が放熱内部経路を流通する。帰還内部経路は受熱部の下部に設けられ、冷媒が帰還内部経路を流通する。フィン部は、放熱内部経路と帰還内部経路との間に設けられる。流出口は、放熱経路と放熱内部経路とを接続する。流入口は、帰還経路と帰還内部経路とを接続する。仕切壁は、受熱部の前面と後面との間に、フィンと平行方向になるように設けられる。受熱器は、仕切壁と受熱部の内壁とで囲まれて形成される。放熱内部経路開口は、仕切壁において、各受熱器の放熱内部経路を連通させる。帰還内部経路開口は、仕切壁において、各受熱器の帰還内部経路を連通させる。流入口と流出口とは、受熱部の同一の側面に設けられる。フィン部は、受熱板から内部に突出し、フィン間の隙間により構成される冷媒の流路が上下方向となるように設けられる。帰還経路側の最下流の受熱器に受熱板を介して設置された発熱体の発熱量は、上流の受熱器に受熱板を介して設置された発熱体の発熱量よりも小さい。このようにして、帰還経路側の最下流の受熱器まで液相の冷媒が行き渡る構成としている。これにより、帰還経路側の下流の受熱器のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱部内を満たす必要が無く、薄い液相の冷媒の層を受熱部内に形成することができ、高い冷却性能を有する。
A cooling device according to an embodiment of the present invention is a cooling device that cools a heating element by a phase change of the refrigerant, and circulates the refrigerant formed by sequentially connecting a heat receiving part, a heat radiation path, a heat radiation part, and a return path. Provide a route. The heat receiving part has a horizontally long rectangular parallelepiped shape with a front surface and a rear surface having a maximum area, a heat receiving plate, a heat dissipation internal path, a return internal path, a fin portion having a plurality of flat fins, an outlet, and an inlet And one or a plurality of partition walls, a plurality of heat receivers, a heat dissipation internal path opening, and a return internal path opening. The heat receiving plate is provided with a plurality of heating elements on at least one of the front surface and the rear surface. The heat dissipation internal path is provided in the upper part of the heat receiving part, and the refrigerant flows through the heat dissipation internal path. The return internal path is provided below the heat receiving part, and the refrigerant flows through the return internal path. The fin portion is provided between the heat dissipation internal path and the return internal path. The outflow port connects the heat dissipation path and the heat dissipation internal path. The inflow port connects the return path and the return internal path. The partition wall is provided between the front surface and the rear surface of the heat receiving unit so as to be parallel to the fins. The heat receiver is formed by being surrounded by the partition wall and the inner wall of the heat receiving portion. The heat radiation internal path opening communicates the heat radiation internal path of each heat receiver in the partition wall. The return internal path opening communicates the return internal path of each heat receiver in the partition wall. The inflow port and the outflow port are provided on the same side surface of the heat receiving unit. The fin portion protrudes inward from the heat receiving plate, and is provided so that the refrigerant flow path constituted by the gap between the fins is in the vertical direction. The calorific value of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is smaller than the calorific value of the heating element installed in the upstream heat receiver via the heat receiving plate. In this way, the liquid-phase refrigerant spreads to the most downstream heat receiver on the return path side. Thereby, the dry-out of the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
すなわち、帰還経路の液相の冷媒は、流入口から帰還内部経路に流入し、帰還内部経路からフィン部に流出する。そして、フィン部に流出した液相の冷媒は、フィンを介して発熱体から発生した熱を受熱し、気相と液相との二相の冷媒となり、圧力が高い状態となる。これは、冷媒が気化するときに、冷媒の体積が膨張するためである。
That is, the liquid-phase refrigerant in the return path flows into the return internal path from the inflow port, and flows out from the return internal path to the fin portion. Then, the liquid-phase refrigerant that has flowed out to the fin portion receives heat generated from the heating element via the fins, becomes a two-phase refrigerant of a gas phase and a liquid phase, and is in a high pressure state. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
帰還経路側の最下流の受熱器に受熱板を介して設置された発熱体の発熱量は、上流の受熱器に受熱板を介して設置された発熱体の発熱量よりも小さい構成としている。そのため、最下流の受熱器の温度は、上流側の受熱器の温度より低温となる。そのため、最下流の受熱器においては、上流側の受熱器より冷媒が受熱する熱量が少ないため、液相の冷媒が気化して膨張する冷媒の体積も少ない。従って、最下流の受熱器内の圧力は、上流側の受熱器内の圧力より低くなる。これにより、冷媒は、圧力の低い最下流の受熱器に流れやすくなる。そのため、帰還経路側の下流の受熱器において、ドライアウトが抑制される。
The heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is configured to be smaller than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate. Therefore, the temperature of the most downstream heat receiver is lower than the temperature of the upstream heat receiver. Therefore, in the most downstream heat receiver, since the amount of heat received by the refrigerant is smaller than that of the upstream heat receiver, the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant is also small. Accordingly, the pressure in the most downstream heat receiver is lower than the pressure in the upstream heat receiver. Thereby, a refrigerant | coolant becomes easy to flow into the downstream most heat receiving device with a low pressure. Therefore, dryout is suppressed in the downstream heat receiver on the return path side.
以上のようにして、帰還経路側の最下流の受熱板に設置される発熱体の発熱量は、上流に設置される発熱体の発熱量よりも小さい構成としている。これにより、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱部内を満たす必要が無く、薄い液相の冷媒の層を受熱部内に形成することができ、高い冷却性能を有する。
As described above, the heating value of the heating element installed on the most downstream heat receiving plate on the return path side is configured to be smaller than the heating value of the heating element installed upstream. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
また、受熱部は、帰還内部経路とフィン部との間に、受熱部の底面と平行になるように設けられた仕切板を備え、仕切板は、複数の開口部を有する構成にしてもよい。
Further, the heat receiving unit may include a partition plate provided between the return internal path and the fin portion so as to be parallel to the bottom surface of the heat receiving unit, and the partition plate may have a plurality of openings. .
帰還内部経路とフィン部との間に設けられた仕切板は、複数の開口部を有するので、帰還経路の液相の冷媒は、流入口から帰還内部経路に流入し、仕切板に設けられた開口部から受熱部内に流出する。各受熱器において、仕切板の開口部のみから液相の冷媒がフィン部に供給されるため、帰還内部経路から液相の冷媒がフィン部に大量に流出することが抑制される。これにより、下流の受熱器において、ドライアウトが抑制される。
Since the partition plate provided between the return internal path and the fin portion has a plurality of openings, the liquid-phase refrigerant in the return path flows into the return internal path from the inlet and is provided in the partition plate. It flows out from the opening into the heat receiving part. In each heat receiver, since the liquid phase refrigerant is supplied to the fin portion only from the opening of the partition plate, a large amount of the liquid phase refrigerant is prevented from flowing out from the return internal path to the fin portion. Thereby, dryout is suppressed in the downstream heat receiver.
以上のようにして、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱器内を満たす必要が無く、薄い液相の冷媒の層を受熱器内に形成することができ、高い冷却性能を有する。
As described above, dry-out in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
また、受熱部は、帰還内部経路に設けられ、冷媒が流通する帰還内部管路を備え、帰還内部経路開口は、仕切壁において、各受熱器の帰還内部管路を連通させ、帰還内部管路は、複数の開口部を有する構成にしてもよい。
The heat receiving section is provided in a return internal path and includes a return internal pipe through which the refrigerant flows, and the return internal path opening communicates with the return internal pipe of each heat receiver in the partition wall. May be configured to have a plurality of openings.
これにより、帰還内部管路は複数の開口部を有するので、帰還経路の液相の冷媒は、流入口から帰還内部管路に流入し、帰還内部管路に設けた開口部から受熱部内に流出する。そして、フィン部に流出した液相の冷媒は、フィンを介して発熱体から発生した熱を受熱し、気相と液相との二相の冷媒となり、圧力が高い状態となる。これは、冷媒が気化するときに、冷媒の体積が膨張するためである。
As a result, since the return internal pipe has a plurality of openings, the liquid-phase refrigerant in the return path flows into the return internal pipe from the inflow port, and flows out into the heat receiving section from the opening provided in the return internal pipe. To do. Then, the liquid-phase refrigerant that has flowed out to the fin portion receives heat generated from the heating element via the fins, becomes a two-phase refrigerant of a gas phase and a liquid phase, and is in a high pressure state. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
帰還経路側の最下流の受熱器に受熱板を介して設置された発熱体の発熱量は、上流の受熱器に受熱板を介して設置された発熱体の発熱量よりも小さい構成としている。そのため、最下流の受熱器の温度は、上流側の受熱器の温度より低温となる。そのため、最下流の受熱器においては、上流側の受熱器より冷媒が受熱する熱量が少ないため、液相の冷媒が気化して膨張する冷媒の体積も少ない。従って、最下流の受熱器内の圧力は、上流側の受熱器内の圧力より低くなる。冷媒は、圧力の低い最下流の受熱器に流れやすくなる。そのため、帰還経路側の最下流の受熱器において、ドライアウトが抑制される。
The heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is configured to be smaller than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate. Therefore, the temperature of the most downstream heat receiver is lower than the temperature of the upstream heat receiver. Therefore, in the most downstream heat receiver, since the amount of heat received by the refrigerant is smaller than that of the upstream heat receiver, the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant is also small. Accordingly, the pressure in the most downstream heat receiver is lower than the pressure in the upstream heat receiver. The refrigerant easily flows to the downstream most downstream heat receiver. Therefore, dryout is suppressed in the most downstream heat receiver on the return path side.
また、液相の冷媒が受熱器の底面を直接流れる構成と比較して、液相の冷媒が帰還内部管路内を流れる構成では、帰還内部管路内に存在する液相の冷媒は受熱器内の熱により加熱されにくい。そのため、上記の構成の冷却装置は、帰還内部管路内において液相の冷媒が気化し、気化した冷媒が帰還経路側に逆流することを、抑制することができる。
In addition, in the configuration in which the liquid-phase refrigerant flows in the return internal conduit compared to the configuration in which the liquid-phase refrigerant flows directly through the bottom surface of the heat receiver, the liquid-phase refrigerant in the return internal conduit is the heat receiver. It is hard to be heated by the heat inside. Therefore, the cooling device having the above-described configuration can suppress the liquid-phase refrigerant from being vaporized in the return internal pipe and preventing the vaporized refrigerant from flowing backward to the return path.
以上のようにして、帰還経路側の最下流の受熱器に受熱板を介して設置される発熱体の発熱量は、上流の受熱器に受熱板を介して設置される発熱体の発熱量よりも小さい構成としている。これにより、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱部内を満たす必要が無く、薄い液相の冷媒の層を受熱部内に形成することができ、高い冷却性能を有する。
As described above, the heat generation amount of the heating element installed in the most downstream heat receiver on the return path side via the heat receiving plate is larger than the heat generation amount of the heating element installed in the upstream heat receiving device via the heat receiving plate. The structure is also small. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
また、各受熱器における仕切板の開口部の合計開口面積は、最上流の受熱器で最も小さく、下流の受熱器になるほど大きくなる構成にしてもよい。
Further, the total opening area of the opening portions of the partition plates in each heat receiver may be the smallest in the most upstream heat receiver, and may be configured to increase as the downstream heat receiver becomes.
帰還内部経路とフィン部との間に設けた仕切板は、複数の開口部を有するので、帰還経路の液相の冷媒は、流入口から帰還内部経路に流入し、仕切板に設けた開口部から受熱部内に流出する。
Since the partition plate provided between the return internal path and the fin portion has a plurality of openings, the liquid phase refrigerant in the return path flows into the return internal path from the inflow port, and the opening provided in the partition plate Out into the heat receiving part.
各受熱器における仕切板の開口部の合計開口面積は、最上流の受熱器で最も小さく、下流の受熱器になるほど大きくなるように構成されている。そのため、最上流の受熱器においては合計開口面積が小さいので、最上流の受熱器における仕切板の開口部から液相の冷媒は流出しにくい。また、下流の受熱器になるほど合計開口面積が大きくなるので、下流の受熱器になるほど仕切板の開口部から液相の冷媒は流出しやすくなる。これにより、下流の受熱器において、ドライアウトが抑制される。
The total opening area of the openings of the partition plates in each heat receiver is configured to be the smallest in the most upstream heat receiver and increase as the downstream heat receiver is reached. Therefore, since the total opening area is small in the most upstream heat receiver, the liquid-phase refrigerant hardly flows out from the opening of the partition plate in the most upstream heat receiver. In addition, since the total opening area increases as the downstream heat receiver becomes, the liquid phase refrigerant tends to flow out from the opening of the partition plate as the downstream heat receiver becomes. Thereby, dryout is suppressed in the downstream heat receiver.
以上のようにして、各受熱器における仕切板の開口部の合計開口面積は、最上流の受熱器で最も小さく、下流の受熱器になるほど大きくなる構成にしてもよい。これにより、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱器内を満たす必要が無く、薄い液相の冷媒の層を受熱器内に形成することができ、高い冷却性能を有する。
As described above, the total opening area of the opening portions of the partition plates in each heat receiver may be the smallest in the most upstream heat receiver and may increase as the downstream heat receiver is increased. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
また、各受熱器における帰還内部管路の開口部の合計開口面積は、最上流の受熱器で最も小さく、下流の受熱器になるほど大きくなる構成にしてもよい。
Further, the total opening area of the opening of the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the downstream heat receiver becomes larger.
帰還内部管路は複数の開口部を有するので、帰還経路の液相の冷媒は、流入口から帰還内部管路に流入し、帰還内部管路に設けた開口部から受熱部内に流出する。
Since the return internal conduit has a plurality of openings, the liquid-phase refrigerant in the return route flows into the return internal conduit from the inlet and flows out into the heat receiving portion from the opening provided in the return internal conduit.
各受熱器における帰還内部管路の開口部の合計開口面積は、最上流の受熱器で最も小さく、下流の受熱器になるほど大きくなるように構成されている。そのため、最上流の受熱器においては合計開口面積が小さいので、最上流の受熱器における帰還内部管路の開口部から液相の冷媒は流出しにくい。また、下流の受熱器になるほど合計開口面積が大きくなるので、下流の受熱器になるほど帰還内部管路の開口部から液相の冷媒は流出しやすくなる。これにより、下流の受熱器において、ドライアウトが抑制される。
The total opening area of the opening of the return internal pipe line in each heat receiver is configured to be the smallest in the most upstream heat receiver and increase as it becomes the downstream heat receiver. Therefore, since the total opening area is small in the most upstream heat receiver, the liquid-phase refrigerant hardly flows out from the opening of the return internal pipe line in the most upstream heat receiver. Further, since the total opening area becomes larger as the downstream heat receiver becomes, the liquid-phase refrigerant tends to flow out from the opening of the return internal pipe line as the downstream heat receiver becomes. Thereby, dryout is suppressed in the downstream heat receiver.
以上のようにして、各受熱器における帰還内部管路の開口部の合計開口面積は、最上流の受熱器で最も小さく、下流の受熱器になるほど大きくなる構成にしてもよい。これにより、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱器内を満たす必要が無く、薄い液相の冷媒の層を受熱器内に形成することができ、高い冷却性能を有する。
As described above, the total opening area of the opening portion of the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver and may be increased as the downstream heat receiver is reached. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
また、各受熱器における仕切板の開口部の個数は、最上流の受熱器で最も少なく、下流の受熱器になるほど多くなる構成にしてもよい。
Further, the number of openings of the partition plate in each heat receiver may be the smallest in the most upstream heat receiver and may be increased as the downstream heat receiver is reached.
これにより、最上流の受熱器における仕切板の開口部の個数が最も少ないので、最上流の受熱器における仕切板の開口部から液相の冷媒は流出しにくい。また、下流の受熱器になるほど仕切板の開口部の個数が多くなるので、下流の受熱器になるほど仕切板の開口部から液相の冷媒は流出しやすくなる。これにより、下流の受熱器において、ドライアウトが抑制される。
Thereby, since the number of openings of the partition plate in the most upstream heat receiver is the smallest, the liquid-phase refrigerant hardly flows out from the opening of the partition plate in the most upstream heat receiver. In addition, since the number of openings of the partition plate increases as the downstream heat receiver becomes, the liquid phase refrigerant tends to flow out from the opening of the partition plate as the downstream heat receiver becomes. Thereby, dryout is suppressed in the downstream heat receiver.
以上のようにして、各受熱器における仕切板の開口部の個数は、最上流の受熱器で最も少なく、下流の受熱器になるほど多くなる構成にしてもよい。これにより、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱器内を満たす必要が無く、薄い液相の冷媒の層を受熱器内に形成することができ、高い冷却性能を有する。
As described above, the number of openings of the partition plate in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the number of downstream heat receivers increases. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
また、各受熱器における帰還内部管路の開口部の個数は、最上流の受熱器で最も少なく、下流の受熱器になるほど多くなる構成にしてもよい。
In addition, the number of openings of the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the number of downstream heat receivers increases.
これにより、最上流の受熱器における帰還内部管路の開口部の個数が最も少ないので、最上流の受熱器における帰還内部管路の開口部から液相の冷媒は流出しにくい。また、下流の受熱器になるほど帰還内部管路の開口部の個数が多くなるので、下流の受熱器になるほど帰還内部管路の開口部から液相の冷媒は流出しやすくなる。これにより、下流の受熱器において、ドライアウトが抑制される。
Thereby, since the number of openings in the return internal conduit in the most upstream heat receiver is the smallest, the liquid-phase refrigerant hardly flows out from the opening in the return internal conduit in the most upstream heat receiver. In addition, since the number of openings in the return internal pipe increases as the heat receiver becomes downstream, the liquid-phase refrigerant tends to flow out from the opening of the return internal pipe as the heat sink becomes downstream. Thereby, dryout is suppressed in the downstream heat receiver.
以上のようにして、各受熱器における帰還内部管路の開口部の個数は、最上流の受熱器で最も少なく、下流の受熱器になるほど多くなる構成にしてもよい。これにより、帰還経路側の下流の受熱器内のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱器内を満たす必要が無く、薄い液相の冷媒の層を受熱器内に形成することができ、高い冷却性能を有する。
As described above, the number of openings in the return internal pipe line in each heat receiver may be the smallest in the most upstream heat receiver, and may increase as the number of downstream heat receivers increases. Thereby, the dryout in the downstream heat receiver on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiver with an excessive amount of liquid-phase refrigerant, and can form a thin liquid-phase refrigerant layer in the heat receiver, resulting in high cooling performance. Have.
また、発熱体は、受熱部の底面から距離を置いて受熱板に設置される構成にしてもよい。
The heating element may be installed on the heat receiving plate at a distance from the bottom surface of the heat receiving unit.
これにより、発熱体は、受熱部の底面から距離を置いて受熱板に設置される構成とするため、受熱部の下部に設けた帰還内部経路内を流れる液相の冷媒、すなわち、受熱部の底面を流れる液相の冷媒は、発熱体から距離を置くこととなる。そのため、液相の冷媒は、発熱体から受熱しにくくなる。そのため、帰還内部経路内を流れる液相の冷媒が受熱して気相の冷媒となり、フィン部に流出して帰還内部経路の下流まで液相の冷媒が行き渡らない状態が抑制される。これにより、帰還経路側の受熱部の下流において、ドライアウトが抑制される。
Thus, the heating element is configured to be installed on the heat receiving plate at a distance from the bottom surface of the heat receiving part, so that the liquid phase refrigerant flowing in the return internal path provided at the lower part of the heat receiving part, that is, the heat receiving part The liquid refrigerant flowing through the bottom surface is spaced from the heating element. Therefore, the liquid phase refrigerant is less likely to receive heat from the heating element. Therefore, the liquid-phase refrigerant flowing in the return internal path receives heat and becomes a gas-phase refrigerant, and a state where the liquid-phase refrigerant does not reach the downstream of the return internal path through the fin portion is suppressed. Thereby, dryout is suppressed downstream of the heat receiving part on the return path side.
以上のようにして、発熱体は、受熱部の底面から距離を置いて受熱板に設置される構成にしてもよい。これにより、帰還経路側の受熱部の下流のドライアウトが抑制される。すなわち、上記の構成の冷却装置は、過剰な量の液相の冷媒で受熱部内を満たす必要が無く、薄い液相の冷媒の層を受熱部内に形成することができ、高い冷却性能を有する。
As described above, the heating element may be installed on the heat receiving plate at a distance from the bottom surface of the heat receiving unit. Thereby, the dry-out downstream of the heat receiving part on the return path side is suppressed. That is, the cooling device having the above configuration does not need to fill the heat receiving portion with an excessive amount of liquid phase refrigerant, can form a thin liquid phase refrigerant layer in the heat receiving portion, and has high cooling performance.
また、本発明の一実施形態に係る電子機器は、上記の構成の冷却装置を搭載してもよい。これにより、上記の構成の電子機器は、高い冷却性能を有する冷却装置を搭載するため、安定して動作できる。
Moreover, the electronic apparatus according to an embodiment of the present invention may be equipped with the cooling device having the above-described configuration. As a result, the electronic device having the above-described configuration can operate stably because it is equipped with a cooling device having high cooling performance.
(実施の形態1)
以下、実施の形態1について、図面を参照しながら説明する。 (Embodiment 1)
Hereinafter,Embodiment 1 will be described with reference to the drawings.
以下、実施の形態1について、図面を参照しながら説明する。 (Embodiment 1)
Hereinafter,
図1は、実施の形態1の冷却装置を搭載した電子機器の概略図である。
FIG. 1 is a schematic diagram of an electronic device equipped with the cooling device of the first embodiment.
図1に示すように、電子機器50は、ケース51内に第1の発熱体群28、第2の発熱体群29および冷却装置1を搭載している。第1の発熱体群28および第2の発熱体群29は、複数の発熱体から構成されている。第1の発熱体群28および第2の発熱体群29は、例えば、電力用半導体素子、中央演算処理装置(CPU)、大規模集積回路(LSI)、絶縁ゲートバイポーラトランジスタ(IGBT)、ダイオード等の発熱体で構成されていてよい。
As shown in FIG. 1, the electronic device 50 has a first heating element group 28, a second heating element group 29, and a cooling device 1 mounted in a case 51. The first heating element group 28 and the second heating element group 29 are composed of a plurality of heating elements. The first heating element group 28 and the second heating element group 29 include, for example, a power semiconductor element, a central processing unit (CPU), a large scale integrated circuit (LSI), an insulated gate bipolar transistor (IGBT), a diode, and the like. The heating element may be configured.
冷却装置1は、冷媒の相変化によって第1の発熱体群28および第2の発熱体群29を冷却する。冷却装置1は、受熱部3、放熱経路5、放熱部4および帰還経路6を順に連結して形成される冷媒の循環経路を備える。この構成により、冷却装置1が備える循環経路は内部が密閉空間となる。図1では図示していないが、循環経路内は、減圧された上で、冷媒が封入されている。冷媒としては、フロン類、フッ素系溶剤類などが用いられるが、これらに限られない。受熱部3、放熱部4および後述するフィンである第1のフィン22、第2のフィン23の材質は、アルミニウムが適しているが、これに限られない。
The cooling device 1 cools the first heating element group 28 and the second heating element group 29 by the phase change of the refrigerant. The cooling device 1 includes a refrigerant circulation path formed by sequentially connecting the heat receiving section 3, the heat radiation path 5, the heat radiation section 4, and the return path 6. With this configuration, the inside of the circulation path provided in the cooling device 1 is a sealed space. Although not shown in FIG. 1, the refrigerant is sealed in the circulation path after the pressure is reduced. As the refrigerant, chlorofluorocarbons, fluorinated solvents and the like are used, but are not limited thereto. Aluminum is suitable for the material of the heat receiving part 3, the heat radiating part 4, and the first fin 22 and the second fin 23, which will be described later, but is not limited thereto.
冷却装置1は、第1の発熱体群28および第2の発熱体群29の熱によって気化した冷媒を冷却するための水冷チラー(図示なし)に接続されている。水冷チラーで冷却された冷却水は、冷却水供給経路7から放熱部4に供給される。そして、気化した冷媒は、放熱部4において水冷チラーの冷却水と熱交換することにより、冷却されて液化する。熱交換した冷却水は、冷却水戻り経路8を経て水冷チラーに戻り、水冷チラーにおいて冷却される。
The cooling device 1 is connected to a water cooling chiller (not shown) for cooling the refrigerant vaporized by the heat of the first heating element group 28 and the second heating element group 29. The cooling water cooled by the water cooling chiller is supplied from the cooling water supply path 7 to the heat radiating unit 4. The vaporized refrigerant is cooled and liquefied by exchanging heat with the cooling water of the water-cooled chiller in the heat radiating section 4. The heat-exchanged cooling water returns to the water-cooled chiller via the cooling water return path 8 and is cooled in the water-cooled chiller.
本実施の形態では、冷媒の冷却方法は、水冷チラーによる水冷式としたが、冷却ファンによる空冷式やその他の方式としてもよい。
In the present embodiment, the cooling method of the refrigerant is a water cooling method using a water cooling chiller, but an air cooling method using a cooling fan or other methods may be used.
次に、上記の構成における冷却装置1の基本的な仕組みについて説明する。
Next, the basic mechanism of the cooling device 1 having the above configuration will be described.
冷却装置1が備える循環経路は、内部を減圧した後に冷媒を封入したものである。循環経路内の圧力は、冷媒の作用により外部温度に応じた冷媒の飽和圧力となる。第1の発熱体群28および第2の発熱体群29の熱は受熱部3を介して冷媒に伝わり、液相の冷媒が気化することで、第1の発熱体群28および第2の発熱体群29が冷却される。受熱部3内にて気化した冷媒は、気化されていない液相の冷媒との気液二相の混相流となって、受熱部3から放熱経路5を通り放熱部4へと移動する。そして、気化した冷媒は、冷却水供給経路7から供給された水冷チラーの冷却水により冷却され、再び液相の冷媒となり、帰還経路6を経て受熱部3に戻る。
The circulation path provided in the cooling device 1 is one in which a refrigerant is sealed after the inside is depressurized. The pressure in the circulation path becomes the saturation pressure of the refrigerant according to the external temperature by the action of the refrigerant. The heat of the first heating element group 28 and the second heating element group 29 is transmitted to the refrigerant through the heat receiving portion 3, and the liquid refrigerant is vaporized, whereby the first heating element group 28 and the second heating element group 28 are heated. The body group 29 is cooled. The refrigerant vaporized in the heat receiving part 3 becomes a gas-liquid two-phase mixed flow with the liquid refrigerant not vaporized, and moves from the heat receiving part 3 to the heat radiating part 4 through the heat radiation path 5. The vaporized refrigerant is cooled by the cooling water of the water-cooled chiller supplied from the cooling water supply path 7, becomes a liquid-phase refrigerant again, and returns to the heat receiving unit 3 through the return path 6.
よって、受熱部3内にて液相の冷媒が気化し、気化した冷媒が放熱経路5を通過して放熱部4にて冷却されて液化し、液化した冷媒が帰還経路6を通過して再び受熱部3内に供給されるサイクルが繰り返される。これにより、冷却装置1は、第1の発熱体群28および第2の発熱体群29を冷却している。
Therefore, the liquid-phase refrigerant is vaporized in the heat receiving part 3, the vaporized refrigerant passes through the heat radiation path 5 and is cooled and liquefied in the heat radiation part 4, and the liquefied refrigerant passes through the feedback path 6 and again. The cycle supplied into the heat receiving unit 3 is repeated. Thereby, the cooling device 1 cools the first heating element group 28 and the second heating element group 29.
帰還経路6の径は、放熱経路5の径より小さい。これにより、帰還経路6の流路圧損が放熱経路5の流路圧損より高くなるので、冷媒が受熱部3から帰還経路6に逆流することが抑制される。
The diameter of the return path 6 is smaller than the diameter of the heat dissipation path 5. Thereby, since the flow path pressure loss of the return path 6 becomes higher than the flow path pressure loss of the heat radiation path 5, the refrigerant is prevented from flowing back from the heat receiving portion 3 to the return path 6.
図2は、実施の形態1の冷却装置1の受熱部3の外観を示す図である。
FIG. 2 is a diagram illustrating an appearance of the heat receiving unit 3 of the cooling device 1 according to the first embodiment.
図3および図4は、実施の形態1の冷却装置1の受熱部3の分解斜視図である。
3 and 4 are exploded perspective views of the heat receiving unit 3 of the cooling device 1 according to the first embodiment.
図5は、実施の形態1の冷却装置の受熱部3の第1の受熱板15を外して前面側から見た図である。
FIG. 5 is a view of the first heat receiving plate 15 of the heat receiving unit 3 of the cooling device according to the first embodiment as viewed from the front side.
図2、図3および図4に示すように、受熱部3は、前面および後面が最大面積の横長の直方体形状である。
As shown in FIG. 2, FIG. 3, and FIG. 4, the heat receiving part 3 has a horizontally long rectangular parallelepiped shape with the maximum area on the front and rear surfaces.
受熱部3は、前面および後面が垂直方向と平行になるように設置される。受熱部3は、前面に第1の受熱板15を備え、後面に第2の受熱板16を備える。第1の受熱板15には第1の発熱体群28(図1参照)が設置され、第2の受熱板16には第2の発熱体群29(図1参照)が設置される。
The heat receiving unit 3 is installed so that the front surface and the rear surface are parallel to the vertical direction. The heat receiving unit 3 includes a first heat receiving plate 15 on the front surface and a second heat receiving plate 16 on the rear surface. The first heat receiving plate 15 is provided with a first heating element group 28 (see FIG. 1), and the second heat receiving plate 16 is provided with a second heating element group 29 (see FIG. 1).
なお、発熱体、受熱板、フィン他をそれぞれ第1と第2とに分けているが、これは、各々が2つずつあることを意味し、特に記載がないかぎり第1と第2とに違いはない。
In addition, although a heat generating body, a heat receiving plate, a fin, etc. are each divided into the first and second, this means that there are two each, and unless otherwise specified, the first and second There is no difference.
また、本実施の形態では、受熱部3は、発熱体群および受熱板をそれぞれ2つずつ備えているが、前面または後面のいずれか一方に第1の発熱体群28が設置された第1の受熱板15のみを備えてもよい(図示せず)。
Further, in the present embodiment, the heat receiving section 3 includes two heating element groups and two heat receiving plates, respectively, but the first heating element group 28 is provided on either the front surface or the rear surface. Only the heat receiving plate 15 may be provided (not shown).
図5に示すように、第2の発熱体群29は、第1の発熱体43、第2の発熱体44および第3の発熱体45から構成されている。第2の発熱体群29を構成する各発熱体を第2の受熱板16に接触させて、各発熱体と第2の受熱板16とを熱的に接続している。図示しないが、第1の発熱体群28も、複数の発熱体から構成されている。第1の発熱体群28を構成する各発熱体を第1の受熱板15に接触させて、各発熱体と第1の受熱板15とを熱的に接続している。第1の受熱板15および第2の受熱板16には、各発熱体群を固定するための固定用ネジ孔19が適宜設けられている。これにより、第1の受熱板15に第1の発熱体群28を、第2の受熱板16に第2の発熱体群29をネジで固定することができる。第1の発熱体群28および第2の発熱体群29は、その間に受熱部3が挟まれるように垂直方向と平行になるように設置される。
As shown in FIG. 5, the second heating element group 29 is composed of a first heating element 43, a second heating element 44, and a third heating element 45. Each heating element constituting the second heating element group 29 is brought into contact with the second heat receiving plate 16 to thermally connect each heating element and the second heat receiving plate 16. Although not shown, the first heating element group 28 is also composed of a plurality of heating elements. Each heating element constituting the first heating element group 28 is brought into contact with the first heat receiving plate 15 to thermally connect each heating element and the first heat receiving plate 15. The first heat receiving plate 15 and the second heat receiving plate 16 are appropriately provided with fixing screw holes 19 for fixing the heating element groups. Thus, the first heat generating group 28 can be fixed to the first heat receiving plate 15 and the second heat generating group 29 can be fixed to the second heat receiving plate 16 with screws. The first heating element group 28 and the second heating element group 29 are installed so as to be parallel to the vertical direction so that the heat receiving portion 3 is sandwiched therebetween.
横長の直方体形状である受熱部3の上部には、放熱内部経路25として空間が設けられている。また、受熱部3の下部には、帰還内部経路24として空間が設けられている。すなわち、受熱部3は、放熱内部経路25と帰還内部経路24とを備える。冷媒は、放熱内部経路25および帰還内部経路24を流通する。
A space is provided as a heat radiating internal path 25 at the top of the heat receiving portion 3 having a horizontally long rectangular parallelepiped shape. In addition, a space is provided as a return internal path 24 below the heat receiving unit 3. That is, the heat receiving unit 3 includes a heat dissipation internal path 25 and a return internal path 24. The refrigerant flows through the heat dissipation internal path 25 and the return internal path 24.
受熱部3は、放熱内部経路25と帰還内部経路24との間の中央部に設けられるフィン部2を備える。
The heat receiving portion 3 includes a fin portion 2 provided at a central portion between the heat dissipation internal path 25 and the return internal path 24.
受熱部3は、放熱経路5と放熱内部経路25とを接続する流出口31と、帰還経路6と帰還内部経路24とを接続する流入口30とを備える。
The heat receiving unit 3 includes an outlet 31 that connects the heat dissipation path 5 and the heat dissipation internal path 25, and an inlet 30 that connects the return path 6 and the return internal path 24.
流出口31と流入口30とは、受熱部3の同一の側面に設けられる。流出口31と流入口30とが設けられる側面は、第1の受熱板15および第2の受熱板16が設けられる前面および後面をつなぐ側面である。
The outlet 31 and the inlet 30 are provided on the same side surface of the heat receiving unit 3. The side surface on which the outflow port 31 and the inflow port 30 are provided is a side surface that connects the front surface and the rear surface on which the first heat receiving plate 15 and the second heat receiving plate 16 are provided.
フィン部2は、複数の平板状の第1のフィン22と、複数の平板状の第2のフィン23とを有する。第1のフィン22は、第1の受熱板15から受熱部3の内部に突出し、第1のフィン22間の隙間により構成される冷媒の流路が上下方向となるように設けられる。第2のフィン23は、第2の受熱板16から受熱部3の内部に突出し、第2のフィン23間の隙間により構成される冷媒の流路が上下方向となるように設けられる。
The fin part 2 has a plurality of flat first fins 22 and a plurality of flat second fins 23. The first fin 22 protrudes from the first heat receiving plate 15 to the inside of the heat receiving portion 3, and is provided so that the refrigerant flow path constituted by the gap between the first fins 22 is in the vertical direction. The second fin 23 protrudes from the second heat receiving plate 16 to the inside of the heat receiving portion 3, and is provided so that the refrigerant flow path constituted by the gap between the second fins 23 is in the vertical direction.
受熱部3は、帰還内部経路24とフィン部2との間に、受熱部3の底面と平行になるように設けられた仕切板32を備える。
The heat receiving unit 3 includes a partition plate 32 provided between the return internal path 24 and the fin portion 2 so as to be parallel to the bottom surface of the heat receiving unit 3.
仕切板32は、複数の開口部33を有する。
The partition plate 32 has a plurality of openings 33.
受熱部3は、受熱部3の前面と後面との間に、すなわち、第1の受熱板15と第2の受熱板16との間に、第1のフィン22および第2のフィン23と平行方向になるように設けられる1または複数の仕切壁34を備える。本実施の形態では、受熱部3は、仕切壁34を2つ備えている。仕切壁34は、受熱部3の長手方向を略等分に区切るように設けられる。受熱部3は、仕切壁34と受熱部3の内壁とで囲まれて形成される区画である複数の受熱器11を備える。本実施の形態では、3つの受熱器11が形成されている。
The heat receiving unit 3 is parallel to the first fin 22 and the second fin 23 between the front surface and the rear surface of the heat receiving unit 3, that is, between the first heat receiving plate 15 and the second heat receiving plate 16. One or a plurality of partition walls 34 are provided so as to be oriented. In the present embodiment, the heat receiving unit 3 includes two partition walls 34. The partition wall 34 is provided so as to divide the longitudinal direction of the heat receiving unit 3 into approximately equal parts. The heat receiving unit 3 includes a plurality of heat receivers 11 that are sections formed by being surrounded by the partition wall 34 and the inner wall of the heat receiving unit 3. In the present embodiment, three heat receivers 11 are formed.
受熱部3は、仕切壁34において、各受熱器11の放熱内部経路25を連通させる放熱内部経路開口35を備える。また、受熱部3は、仕切壁34において、各受熱器11の帰還内部経路24を連通させる帰還内部経路開口36を備える。放熱内部経路開口35および帰還内部経路開口36は、仕切壁34に実際に設けられた開口部であってもよいし、放熱内部経路25および帰還内部経路24を避けて仕切壁34を設ける構造としたものであってもよい。
The heat receiving unit 3 includes a heat radiating internal path opening 35 that communicates the heat radiating internal path 25 of each heat receiver 11 in the partition wall 34. Further, the heat receiving unit 3 includes a return internal path opening 36 that communicates the return internal path 24 of each heat receiver 11 in the partition wall 34. The heat dissipating internal path opening 35 and the return internal path opening 36 may be openings actually provided in the partition wall 34, or the structure in which the partition wall 34 is provided avoiding the heat dissipating internal path 25 and the return internal path 24. It may be what you did.
仕切板32は、複数の開口部33を有する。開口部33は、1つの受熱器11に少なくとも1つ以上設けられている。
The partition plate 32 has a plurality of openings 33. At least one opening 33 is provided in one heat receiver 11.
次に、仕切壁34について説明する。
Next, the partition wall 34 will be described.
流入口30および流出口31が設置された側面側は流出口31に接続している放熱部4の作用により圧力が低い。そのため、受熱部3内においてフィン部2に流出した冷媒は、圧力が低い流入口30および流出口31が設置された側面側に流れやすい。本実施の形態のように、1つの受熱板に複数の発熱体が設けられる場合は、受熱部3の横幅を大きくする場合がある。このような場合、流入口30および流出口31が設置された側面と、その対向する側面までの距離が長くなる。そのため、受熱部3の横幅が小さい場合と比較して、流入口30および流出口31が設置された側面から遠い領域が多くなり、ドライアウトしやすい領域が多くなってしまう。そこで、受熱部3内を仕切壁34により仕切ることにより、仕切られた区画である受熱器11に供給された冷媒は、その受熱器11内の第1のフィン22および第2のフィン23を流れる。そして、冷媒は、第1のフィン22および第2のフィン23と熱交換した後に放熱内部経路25および仕切壁34に設けられた放熱内部経路開口35を通って、放熱経路5側に流れる。従って、受熱部3の横幅が大きい場合であっても、受熱部3内を仕切壁34により仕切ることにより、流入口30および流出口31が設置された側面から遠い領域でのドライアウトが抑制される。
On the side surface side where the inlet 30 and the outlet 31 are installed, the pressure is low due to the action of the heat radiating unit 4 connected to the outlet 31. Therefore, the refrigerant that has flowed out into the fin portion 2 in the heat receiving portion 3 tends to flow to the side surface where the inlet 30 and the outlet 31 having a low pressure are installed. When a plurality of heating elements are provided on one heat receiving plate as in the present embodiment, the lateral width of the heat receiving unit 3 may be increased. In such a case, the distance from the side surface where the inflow port 30 and the outflow port 31 are installed to the opposite side surface becomes longer. Therefore, compared with the case where the horizontal width of the heat receiving part 3 is small, the area far from the side surface on which the inflow port 30 and the outflow port 31 are installed increases, and the area that is easily dried out increases. Therefore, by partitioning the inside of the heat receiving section 3 with the partition wall 34, the refrigerant supplied to the heat receiver 11 that is a partitioned section flows through the first fin 22 and the second fin 23 in the heat receiver 11. . Then, after the heat exchange with the first fins 22 and the second fins 23, the refrigerant flows to the heat dissipation path 5 side through the heat dissipation internal path 25 and the heat dissipation internal path opening 35 provided in the partition wall 34. Therefore, even when the lateral width of the heat receiving part 3 is large, by partitioning the heat receiving part 3 with the partition wall 34, dryout in a region far from the side surface where the inlet 30 and the outlet 31 are installed is suppressed. The
次に、本実施の形態における特徴的な構成について説明する。
Next, a characteristic configuration in the present embodiment will be described.
図5に示すように、第2の受熱板16には、第1の発熱体43、第2の発熱体44および第3の発熱体45から構成される第2の発熱体群29が設置されている。ここで、帰還経路6側の最下流の受熱器21に第2の受熱板16を介して設置された第3の発熱体45の発熱量は、上流の受熱器11(最上流の受熱器20を含む)に第2の受熱板16を介して設置された第1の発熱体43および第2の発熱体44の各発熱量よりも小さい。
As shown in FIG. 5, the second heat receiving plate 16 is provided with a second heating element group 29 including a first heating element 43, a second heating element 44, and a third heating element 45. ing. Here, the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiver 11 (the most upstream heat receiver 20. The amount of heat generated by each of the first heating element 43 and the second heating element 44 installed via the second heat receiving plate 16 is smaller.
すなわち、第2の受熱板16において、帰還経路6側から見た冷媒の流れの最下流に設置される第3の発熱体45の発熱量は、最下流よりも上流に設置される第1の発熱体43および第2の発熱体44の各発熱量よりも小さい。
That is, in the second heat receiving plate 16, the amount of heat generated by the third heating element 45 installed on the most downstream side of the refrigerant flow viewed from the return path 6 side is the first installed on the upstream side of the most downstream side. It is smaller than each calorific value of the heating element 43 and the second heating element 44.
ここで、上流とは、帰還経路6に近い側を意味し、下流とは、帰還経路6から遠い側を意味する。すなわち、最上流の受熱器20とは、各受熱器11のうち帰還経路6に最も近い受熱器である。また、最下流の受熱器21とは、各受熱器11のうち帰還経路6から最も遠い受熱器である。
Here, upstream means the side closer to the return path 6, and downstream means the side far from the return path 6. That is, the most upstream heat receiver 20 is a heat receiver closest to the return path 6 among the heat receivers 11. The most downstream heat receiver 21 is a heat receiver farthest from the return path 6 among the heat receivers 11.
帰還内部経路24とフィン部2との間に、受熱部3の底面と平行になるように設けられた仕切板32は、複数の開口部33を有する。そのため、帰還経路6の液相の冷媒は、流入口30から帰還内部経路24に流入し、仕切板32に設けられた開口部33からフィン部2に流出する。そして、フィン部2に流出した液相の冷媒は、第2のフィン23を介して上流側に設置された第1の発熱体43から発生した熱を受熱し、気相と液相との二相の冷媒となり、圧力が高い状態となる。これは、冷媒が気化するときに、冷媒の体積が膨張するためである。
The partition plate 32 provided between the return internal path 24 and the fin portion 2 so as to be parallel to the bottom surface of the heat receiving portion 3 has a plurality of openings 33. Therefore, the liquid-phase refrigerant in the return path 6 flows into the return internal path 24 from the inflow port 30, and flows out from the opening 33 provided in the partition plate 32 to the fin portion 2. Then, the liquid-phase refrigerant that has flowed out to the fin portion 2 receives heat generated from the first heating element 43 installed on the upstream side via the second fin 23, and the two phases of the gas phase and the liquid phase are received. It becomes a refrigerant of the phase, and the pressure becomes high. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
帰還経路6側の最下流の受熱器21に第2の受熱板16を介して設置された第3の発熱体45の発熱量は、上流の受熱器11(最上流の受熱器20を含む)に第2の受熱板16を介して設置された第1の発熱体43および第2の発熱体44の各発熱量よりも小さい構成としている。そのため、最下流の受熱器21の温度は、上流側の受熱器11(最上流の受熱器20を含む)の温度より低温となる。そのため、最下流の受熱器21においては、上流側の受熱器11(最上流の受熱器20を含む)より冷媒が受熱する熱量が少ないため、液相の冷媒が気化して膨張する冷媒の体積も少ない。従って、最下流の受熱器21内の圧力は、上流側の受熱器11内(最上流の受熱器20を含む)の圧力より低くなる。冷媒は、圧力の低い最下流の受熱器21に流れやすくなる。そのため、帰還経路6側の最下流の受熱器21において、ドライアウトが抑制される。
The amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is the upstream heat receiver 11 (including the most upstream heat receiver 20). The first heat generating body 43 and the second heat generating body 44 installed through the second heat receiving plate 16 are configured to have a smaller heat generation amount. Therefore, the temperature of the most downstream heat receiver 21 is lower than the temperature of the upstream heat receiver 11 (including the most upstream heat receiver 20). Therefore, in the most downstream heat receiver 21, since the amount of heat received by the refrigerant is less than that of the upstream heat receiver 11 (including the most upstream heat receiver 20), the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant. There are few. Therefore, the pressure in the most downstream heat receiver 21 is lower than the pressure in the upstream heat receiver 11 (including the most upstream heat receiver 20). The refrigerant easily flows to the most downstream heat receiver 21 having a low pressure. Therefore, dryout is suppressed in the most downstream heat receiver 21 on the return path 6 side.
以上のようにして、帰還経路6側の最下流の受熱器21に第2の受熱板16を介して設置された第3の発熱体45の発熱量は、上流の受熱器11(最上流の受熱器20を含む)に第2の受熱板16を介して設置された第1の発熱体43および第2の発熱体44の各発熱量よりも小さい構成としている。これにより、最下流の受熱器21内のドライアウトが抑制される。すなわち、冷却装置1は、過剰な量の液相の冷媒で受熱部3内を満たす必要が無く、薄い液相の冷媒の層を受熱部3内に形成することができ、高い冷却性能を有する。
As described above, the amount of heat generated by the third heating element 45 installed in the most downstream heat receiving device 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiving device 11 (the most upstream heat receiving device 11). The heat generation amount of each of the first heat generating body 43 and the second heat generating body 44 installed in the heat receiving device 20 via the second heat receiving plate 16 is smaller. Thereby, the dry-out in the most downstream heat receiver 21 is suppressed. That is, the cooling device 1 does not need to fill the heat receiving unit 3 with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving unit 3, and has high cooling performance. .
また、各受熱器11における仕切板32の開口部33の合計開口面積は、最上流の受熱器20で最も小さく、下流の受熱器11になるほど大きくなる構成にしてもよい。ここで、合計開口面積とは、各受熱器11において、開口部33の開口している箇所の合計面積を意味する。
Further, the total opening area of the openings 33 of the partition plate 32 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may be configured to increase as the downstream heat receiver 11 is reached. Here, the total opening area means the total area of the openings of the opening 33 in each heat receiver 11.
仕切板32は、複数の開口部33を有する。放熱部4で冷却され液化した液相の冷媒は、帰還経路6を流れ、帰還経路6側の最上流の受熱部3の流入口30から帰還内部経路24に流入する。そして、帰還内部経路24に流入した液相の冷媒は、受熱部3を介して第1の発熱体群28および第2の発熱体群29から発生した熱を受熱し、気相と液相との二相の冷媒となり、圧力が高い状態となる。これは、冷媒が気化するときに、冷媒の体積が膨張するためである。この圧力の高い二相の冷媒は、仕切板32の複数の開口部33からフィン部2に流出し、第1のフィン22および第2のフィン23の上下方向の隙間を上方向に流れて、第1のフィン22および第2のフィン23の表面に液相の冷媒を供給する。そして、冷媒は、第1のフィン22および第2のフィン23から受熱しながら、放熱部4の作用で圧力の低い流出口31に放熱内部経路25を通って流れ込む。
The partition plate 32 has a plurality of openings 33. The liquid-phase refrigerant cooled and liquefied by the heat radiating unit 4 flows through the return path 6 and flows into the return internal path 24 from the inlet 30 of the most upstream heat receiving unit 3 on the return path 6 side. The liquid refrigerant flowing into the return internal path 24 receives the heat generated from the first heating element group 28 and the second heating element group 29 via the heat receiving unit 3, and the gas phase, the liquid phase, And the pressure is high. This is because the volume of the refrigerant expands when the refrigerant vaporizes. This high-pressure two-phase refrigerant flows out from the plurality of openings 33 of the partition plate 32 to the fin portion 2, flows upward in the vertical gaps of the first fin 22 and the second fin 23, Liquid phase refrigerant is supplied to the surfaces of the first fin 22 and the second fin 23. Then, while receiving heat from the first fin 22 and the second fin 23, the refrigerant flows into the outlet 31 having a low pressure through the heat radiation internal path 25 by the action of the heat radiation unit 4.
最上流の受熱器20より下流の受熱器11(最下流の受熱器21を含む)においては、液相の冷媒は、帰還経路6から供給されるのではなく、1つ上流の受熱器11から供給される。すなわち、1つ上流の受熱器11内の液相の冷媒が、仕切壁34に設けられた帰還内部経路開口36から受熱器11に供給される。それ以降は、最上流の受熱器20における作用と同様である。
In the heat receiver 11 (including the most downstream heat receiver 21) downstream from the most upstream heat receiver 20, the liquid-phase refrigerant is not supplied from the return path 6, but from one upstream heat receiver 11. Supplied. That is, the liquid-phase refrigerant in the heat receiver 11 that is one upstream is supplied to the heat receiver 11 from the return internal path opening 36 provided in the partition wall 34. The subsequent operation is the same as that in the most upstream heat receiver 20.
各受熱器11における仕切板32の開口部33の合計開口面積は、最上流の受熱器20で最も小さく、下流の受熱器11になるほど大きくなるように構成されている。そのため、最上流の受熱器20においては合計開口面積が小さいので、最上流の受熱器20における仕切板32の開口部33から液相の冷媒は流出しにくい。また、下流の受熱器11になるほど合計開口面積が大きくなるので、下流の受熱器11になるほど仕切板32の開口部33から液相の冷媒は流出しやすくなる。これにより、下流の受熱器11において、ドライアウトが抑制される。
The total opening area of the openings 33 of the partition plate 32 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and increase as the downstream heat receiver 11 is reached. Therefore, since the total opening area is small in the most upstream heat receiver 20, the liquid-phase refrigerant hardly flows out from the opening 33 of the partition plate 32 in the most upstream heat receiver 20. Further, since the total opening area becomes larger as the downstream heat receiver 11 is reached, the liquid phase refrigerant is more likely to flow out from the opening 33 of the partition plate 32 as the downstream heat receiver 11 is reached. Thereby, in the downstream heat receiver 11, dryout is suppressed.
以上のようにして、各受熱器11における仕切板32の開口部33の合計開口面積は、最上流の受熱器20で最も小さく、下流の受熱器11になるほど大きくなるように構成されている。これにより、帰還経路6側の下流の受熱器11内のドライアウトが抑制される。すなわち、冷却装置1は、過剰な量の液相の冷媒で受熱器11内を満たす必要が無く、薄い液相の冷媒の層を受熱器11内に形成することができ、高い冷却性能を有する。
As described above, the total opening area of the openings 33 of the partition plate 32 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and become larger toward the downstream heat receiver 11. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed. In other words, the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
また、各受熱器11における仕切板32の開口部33の個数は、最上流の受熱器20で最も少なく、下流の受熱器11になるほど多くなる構成にしてもよい。これにより、最上流の受熱器20における仕切板32の開口部33の個数が最も少ないので、最上流の受熱器20における仕切板32の開口部33から液相の冷媒は流出しにくい。また、下流の受熱器11になるほど開口部33の個数が多くなるので、下流の受熱器11になるほど仕切板32の開口部33から液相の冷媒は流出しやすくなる。これにより、下流の受熱器11において、ドライアウトが抑制される。
Further, the number of openings 33 of the partition plate 32 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may increase as the number of downstream heat receivers 11 increases. Thereby, since the number of openings 33 of the partition plate 32 in the most upstream heat receiver 20 is the smallest, the liquid-phase refrigerant hardly flows out from the openings 33 of the partition plate 32 in the most upstream heat receiver 20. Further, since the number of the openings 33 increases as the downstream heat receiver 11 is reached, the liquid-phase refrigerant is more likely to flow out from the openings 33 of the partition plate 32 as the downstream heat receiver 11 is reached. Thereby, in the downstream heat receiver 11, dryout is suppressed.
以上のようにして、各受熱器11における開口部33の個数は、最上流の受熱器20で最も少なく、下流の受熱器11になるほど多くなる構成にしてもよい。これにより、帰還経路6側の下流の受熱器11内のドライアウトが抑制される。すなわち、冷却装置1は、過剰な量の液相の冷媒で受熱器11内を満たす必要が無く、薄い液相の冷媒の層を受熱器11内に形成することができ、高い冷却性能を有する。
As described above, the number of the openings 33 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may be increased as the downstream heat receiver 11 is reached. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed. In other words, the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
また、冷却装置1において、第1の発熱体群28および第2の発熱体群29は、受熱部3の底面から距離を置いて、それぞれ第1の受熱板15と第2の受熱板16とに設置される構成にしてもよい。
Further, in the cooling device 1, the first heating element group 28 and the second heating element group 29 are spaced apart from the bottom surface of the heat receiving unit 3 by the first heat receiving plate 15 and the second heat receiving plate 16, respectively. You may make it the structure installed in.
これにより、受熱部3の下部に設けられた帰還内部経路24内を流れる液相の冷媒、すなわち、受熱部3の底面を流れる液相の冷媒は、第1の発熱体群28および第2の発熱体群29から距離を置くこととなる。そのため、冷媒は、第1の発熱体群28および第2の発熱体群29から受熱しにくくなる。そのため、帰還内部経路24内を流れる液相の冷媒が受熱して気相の冷媒となり、フィン部2に流出して帰還内部経路24の下流まで液相の冷媒が行き渡らない状態が抑制される。これにより、帰還経路6側の受熱部3の下流において、ドライアウトが抑制される。
As a result, the liquid-phase refrigerant flowing in the return internal path 24 provided in the lower part of the heat receiving unit 3, that is, the liquid-phase refrigerant flowing in the bottom surface of the heat receiving unit 3, the first heating element group 28 and the second The distance from the heating element group 29 is set. Therefore, the refrigerant hardly receives heat from the first heating element group 28 and the second heating element group 29. Therefore, the liquid-phase refrigerant flowing in the return internal path 24 receives heat and becomes a gas-phase refrigerant, and the state where the liquid-phase refrigerant flows out to the fin portion 2 and does not reach the downstream of the return internal path 24 is suppressed. Thereby, dryout is suppressed downstream of the heat receiving part 3 on the return path 6 side.
以上のようにして、第1の発熱体群28および第2の発熱体群29は、受熱部3の底面から距離を置いて、それぞれ第1の受熱板15と第2の受熱板16とに設置される構成としてもよい。これにより、帰還経路6側の受熱部3の下流のドライアウトが抑制される。すなわち、冷却装置1は、過剰な量の液相の冷媒で受熱部3内を満たす必要が無く、薄い液相の冷媒の層を受熱部3内に形成することができ、高い冷却性能を有する。
As described above, the first heating element group 28 and the second heating element group 29 are separated from the bottom surface of the heat receiving unit 3 by the first heat receiving plate 15 and the second heat receiving plate 16, respectively. It may be configured to be installed. Thereby, the dryout of the downstream of the heat receiving part 3 by the side of the return path 6 is suppressed. That is, the cooling device 1 does not need to fill the heat receiving unit 3 with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving unit 3, and has high cooling performance. .
(実施の形態2)
図6は、実施の形態2の冷却装置1の受熱部3の分解斜視図である。 (Embodiment 2)
FIG. 6 is an exploded perspective view of theheat receiving unit 3 of the cooling device 1 according to the second embodiment.
図6は、実施の形態2の冷却装置1の受熱部3の分解斜視図である。 (Embodiment 2)
FIG. 6 is an exploded perspective view of the
図7は、実施の形態2の冷却装置1の受熱部3の第1の受熱板15を外して前面側から見た図である。
FIG. 7 is a view of the first heat receiving plate 15 of the heat receiving unit 3 of the cooling device 1 according to the second embodiment as viewed from the front side.
実施の形態1と同様の構成要素については同一の符号を付し、その詳細な説明は省略する。
Components similar to those in the first embodiment are denoted by the same reference numerals, and detailed description thereof is omitted.
図6、図7に示すように、受熱部3は、流入口30に接続された帰還内部管路37を備える。帰還内部管路37は帰還内部経路24に設けられ、冷媒は帰還内部管路37を流通する。流入口30は、帰還経路6と帰還内部管路37とを接続する。帰還内部経路開口36は、仕切壁34において、各受熱器11の帰還内部管路37を連通させる。帰還内部管路37は、複数の開口部38を有する。
As shown in FIGS. 6 and 7, the heat receiving unit 3 includes a return internal pipe 37 connected to the inflow port 30. The return internal pipe 37 is provided in the return internal path 24, and the refrigerant flows through the return internal pipe 37. The inflow port 30 connects the return path 6 and the return internal conduit 37. The return internal path opening 36 communicates the return internal pipe line 37 of each heat receiver 11 in the partition wall 34. The return internal conduit 37 has a plurality of openings 38.
受熱部3は、受熱部3の前面と後面との間に、すなわち、第1の受熱板15と第2の受熱板16との間に、第1のフィン22および第2のフィン23と平行方向になるように設けられる1または複数の仕切壁34を備える。本実施の形態では、受熱部3は、仕切壁34を2つ備えている。仕切壁34は、受熱部3の長手方向を略等分に区切るように設けられる。受熱部3は、仕切壁34と受熱部3の内壁とで囲まれて形成される区画である複数の受熱器11を備える。本実施の形態では、3つの受熱器11が形成されている。
The heat receiving unit 3 is parallel to the first fin 22 and the second fin 23 between the front surface and the rear surface of the heat receiving unit 3, that is, between the first heat receiving plate 15 and the second heat receiving plate 16. One or a plurality of partition walls 34 are provided so as to be oriented. In the present embodiment, the heat receiving unit 3 includes two partition walls 34. The partition wall 34 is provided so as to divide the longitudinal direction of the heat receiving unit 3 into approximately equal parts. The heat receiving unit 3 includes a plurality of heat receivers 11 that are sections formed by being surrounded by the partition wall 34 and the inner wall of the heat receiving unit 3. In the present embodiment, three heat receivers 11 are formed.
受熱部3は、仕切壁34において、受熱部3の上部にある、各受熱器11の放熱内部経路25を連通させる放熱内部経路開口35を備える。また、受熱部3は、仕切壁34において、受熱部3の下部にある、各受熱器11の帰還内部管路37を連通させる帰還内部経路開口36を備える。放熱内部経路開口35および帰還内部経路開口36は、仕切壁34に実際に設けられた開口部であってもよいし、放熱内部経路25および帰還内部管路37を避けて仕切壁34を設ける構造としたものであってもよい。
The heat receiving unit 3 includes a heat radiating internal path opening 35 that communicates with the heat radiating internal path 25 of each of the heat receivers 11 at the upper part of the heat receiving unit 3 in the partition wall 34. In addition, the heat receiving unit 3 includes a return internal path opening 36 in the partition wall 34, which is located below the heat receiving unit 3 and communicates with the return internal pipe line 37 of each heat receiver 11. The heat dissipating internal path opening 35 and the return internal path opening 36 may be openings actually provided in the partition wall 34, or the structure in which the partition wall 34 is provided avoiding the heat dissipating internal path 25 and the return internal conduit 37. It may be what.
帰還内部管路37は、複数の開口部38を有する。開口部38は、1つの受熱器11に少なくとも1つ以上設けられている。
The return internal conduit 37 has a plurality of openings 38. At least one opening 38 is provided in one heat receiver 11.
図7に示すように、第2の受熱板16には、第1の発熱体43、第2の発熱体44および第3の発熱体45から構成される第2の発熱体群29が設置されている。ここで、帰還経路6側の最下流の受熱器21に第2の受熱板16を介して設置された第3の発熱体45の発熱量は、上流の受熱器11(最上流の受熱器20を含む)に第1の受熱板15を介して設置された第1の発熱体43および第2の発熱体44の各発熱量よりも小さい。
As shown in FIG. 7, the second heat receiving plate 16 is provided with a second heating element group 29 including a first heating element 43, a second heating element 44, and a third heating element 45. ing. Here, the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiver 11 (the most upstream heat receiver 20. The amount of heat generated by each of the first heat generating body 43 and the second heat generating body 44 installed via the first heat receiving plate 15 is smaller.
すなわち、第2の受熱板16において、帰還経路6側から見た冷媒の流れの最下流に設置される第3の発熱体45の発熱量は、最下流よりも上流に設置される第1の発熱体43および第2の発熱体44の各発熱量よりも小さい。
That is, in the second heat receiving plate 16, the amount of heat generated by the third heating element 45 installed on the most downstream side of the refrigerant flow viewed from the return path 6 side is the first installed on the upstream side of the most downstream side. It is smaller than each calorific value of the heating element 43 and the second heating element 44.
帰還内部管路37は、複数の開口部38を有するので、帰還経路6の液相の冷媒は、流入口30から帰還内部管路37に流入し、帰還内部管路37に設けられた開口部38からフィン部2に流出する。そして、フィン部2に流出した液相の冷媒は、第2のフィン23を介して上流側に設置された第1の発熱体43から発生した熱を受熱し、気相と液相との二相の冷媒となり、圧力が高い状態となる。これは、冷媒が気化するときに、冷媒の体積が膨張するためである。
Since the return internal pipe 37 has a plurality of openings 38, the liquid-phase refrigerant in the return path 6 flows into the return internal pipe 37 from the inlet 30 and is provided in the return internal pipe 37. It flows out from 38 to the fin part 2. Then, the liquid-phase refrigerant that has flowed out to the fin portion 2 receives heat generated from the first heating element 43 installed on the upstream side via the second fin 23, and the two phases of the gas phase and the liquid phase are received. It becomes a refrigerant of the phase, and the pressure becomes high. This is because the volume of the refrigerant expands when the refrigerant vaporizes.
帰還経路6側の最下流の受熱器21に第2の受熱板16を介して設置された第3の発熱体45の発熱量は、上流の受熱器11(最上流の受熱器20を含む)に第2の受熱板16を介して設置された第1の発熱体43および第2の発熱体44の各発熱量よりも小さい構成としている。そのため、最下流の受熱器21の温度は、上流側の受熱器11(最上流の受熱器20を含む)の温度より低温となる。そのため、最下流の受熱器21においては、上流側の受熱器11(最上流の受熱器20を含む)より冷媒が受熱する熱量が少ないため、液相の冷媒が気化して膨張する冷媒の体積も少ない。従って、最下流の受熱器21内の圧力は、上流側の受熱器11内(最上流の受熱器20を含む)の圧力より低くなる。冷媒は、圧力の低い最下流の受熱器21に流れやすくなる。そのため、帰還経路6側の最下流の受熱器21において、ドライアウトが抑制される。
The amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is the upstream heat receiver 11 (including the most upstream heat receiver 20). The first heat generating body 43 and the second heat generating body 44 installed through the second heat receiving plate 16 are configured to have a smaller heat generation amount. Therefore, the temperature of the most downstream heat receiver 21 is lower than the temperature of the upstream heat receiver 11 (including the most upstream heat receiver 20). Therefore, in the most downstream heat receiver 21, since the amount of heat received by the refrigerant is less than that of the upstream heat receiver 11 (including the most upstream heat receiver 20), the volume of the refrigerant that expands by vaporizing the liquid-phase refrigerant. There are few. Therefore, the pressure in the most downstream heat receiver 21 is lower than the pressure in the upstream heat receiver 11 (including the most upstream heat receiver 20). The refrigerant easily flows to the most downstream heat receiver 21 having a low pressure. Therefore, dryout is suppressed in the most downstream heat receiver 21 on the return path 6 side.
また、液相の冷媒が、受熱器11の底面を直接流れる構成と比較して、液相の冷媒が帰還内部管路37内を流れる構成では、帰還内部管路37内に存在する液相の冷媒は受熱器11内の熱により加熱されにくい。そのため、冷却装置1は、帰還内部管路37内において液相の冷媒が気化し、気化した冷媒が帰還経路6側に逆流することを、抑制することができる。
In addition, in the configuration in which the liquid-phase refrigerant flows in the return internal pipe 37 compared to the configuration in which the liquid-phase refrigerant flows directly through the bottom surface of the heat receiver 11, the liquid-phase refrigerant in the return internal pipe 37 The refrigerant is hardly heated by the heat in the heat receiver 11. Therefore, the cooling device 1 can prevent the liquid-phase refrigerant from evaporating in the return internal pipe 37 and flowing back to the return path 6 side.
以上のようにして、帰還経路6側の最下流の受熱器21に第2の受熱板16を介して設置される第3の発熱体45の発熱量は、上流の受熱器11(最上流の受熱器20を含む)に第2の受熱板16を介して設置される第1の発熱体43および第2の発熱体44の各発熱量よりも小さい構成としている。これにより、最下流の受熱器21内のドライアウトが抑制される。すなわち、冷却装置1は、過剰な量の液相の冷媒で受熱部3内を満たす必要が無く、薄い液相の冷媒の層を受熱部3内に形成することができ、高い冷却性能を有する。
As described above, the amount of heat generated by the third heating element 45 installed in the most downstream heat receiver 21 on the return path 6 side via the second heat receiving plate 16 is equal to the upstream heat receiver 11 (the most upstream heat receiver 11). The first heat generating body 43 and the second heat generating body 44 installed in the heat receiving device 20 via the second heat receiving plate 16 are configured to have a smaller heat generation amount. Thereby, the dry-out in the most downstream heat receiver 21 is suppressed. That is, the cooling device 1 does not need to fill the heat receiving unit 3 with an excessive amount of liquid phase refrigerant, and can form a thin liquid phase refrigerant layer in the heat receiving unit 3, and has high cooling performance. .
また、各受熱器11における帰還内部管路37の開口部38の合計開口面積は、最上流の受熱器20で最も小さく、下流の受熱器11になるほど大きくなる構成にしてもよい。
Further, the total opening area of the opening portions 38 of the return internal pipes 37 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may be increased as the downstream heat receiver 11 is reached.
帰還内部管路37は、複数の開口部38を有する。放熱部4で冷却され液化した液相の冷媒は、帰還経路6を流れ、帰還経路6側の最上流の受熱部3の流入口30から帰還内部管路37に流入する。そして、帰還内部管路37に流入した液相の冷媒は、受熱部3を介して第1の発熱体群28および第2の発熱体群29から発生した熱を受熱し、気相と液相との二相の冷媒となり、圧力が高い状態となる。これは、冷媒が気化するときに、冷媒の体積が膨張するためである。この圧力の高い二相の冷媒は、帰還内部管路37の複数の開口部38からフィン部2に流出し、第1のフィン22および第2のフィン23の上下方向の隙間を上方向に流れて、第1のフィン22および第2のフィン23の表面に液相の冷媒を供給する。そして、冷媒は、第1のフィン22および第2のフィン23から受熱しながら、放熱部4の作用で圧力の低い流出口31に放熱内部経路25を通って流れ込む。
The return internal conduit 37 has a plurality of openings 38. The liquid-phase refrigerant cooled and liquefied by the heat radiating unit 4 flows through the return path 6 and flows into the return internal conduit 37 from the inlet 30 of the most upstream heat receiving unit 3 on the return path 6 side. The liquid refrigerant flowing into the return internal pipe 37 receives the heat generated from the first heating element group 28 and the second heating element group 29 via the heat receiving unit 3, and the gas phase and the liquid phase are received. And the pressure is high. This is because the volume of the refrigerant expands when the refrigerant vaporizes. The high-pressure two-phase refrigerant flows out from the plurality of openings 38 of the return internal pipe 37 to the fin portion 2 and flows upward through the vertical gaps of the first fin 22 and the second fin 23. Thus, the liquid-phase refrigerant is supplied to the surfaces of the first fin 22 and the second fin 23. Then, while receiving heat from the first fin 22 and the second fin 23, the refrigerant flows into the outlet 31 having a low pressure through the heat radiation internal path 25 by the action of the heat radiation unit 4.
最上流の受熱器20より下流の受熱器11(最下流の受熱器21を含む)においては、液相の冷媒は、帰還経路6から供給されるのではなく、1つ上流の受熱器11から供給される。すなわち、1つ上流の受熱器11内の帰還内部管路37の液相の冷媒が、仕切壁34に設けられた帰還内部経路開口36を介して下流の受熱器11の帰還内部管路37に供給される。それ以降は、最上流の受熱器20における作用と同様である。
In the heat receiver 11 (including the most downstream heat receiver 21) downstream from the most upstream heat receiver 20, the liquid-phase refrigerant is not supplied from the return path 6, but from one upstream heat receiver 11. Supplied. That is, the liquid-phase refrigerant in the return internal conduit 37 in the upstream heat receiver 11 passes through the return internal passage opening 36 provided in the partition wall 34 to the return internal conduit 37 in the downstream heat receiver 11. Supplied. The subsequent operation is the same as that in the most upstream heat receiver 20.
各受熱器11における帰還内部管路37の開口部38の合計開口面積は、最上流の受熱器20で最も小さく、下流の受熱器11になるほど大きくなるように構成されている。そのため、最上流の受熱器20においては合計開口面積が小さいので、最上流の受熱器20における帰還内部管路37の開口部38から液相の冷媒は流出しにくい。また、下流の受熱器11になるほど合計開口面積が大きくなるので、下流の受熱器11になるほど帰還内部管路37の開口部38から液相の冷媒は流出しやすくなる。これにより、下流の受熱器11において、ドライアウトが抑制される。
The total opening area of the openings 38 of the return internal pipes 37 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and increase as the downstream heat receiver 11 is reached. Therefore, since the total opening area of the most upstream heat receiver 20 is small, the liquid phase refrigerant hardly flows out from the opening 38 of the return internal pipe 37 in the most upstream heat receiver 20. Further, since the total opening area becomes larger as the downstream heat receiver 11 is reached, the liquid phase refrigerant is more likely to flow out from the opening 38 of the return internal pipe 37 as the downstream heat receiver 11 is reached. Thereby, in the downstream heat receiver 11, dryout is suppressed.
以上のようにして、各受熱器11における帰還内部管路37の開口部38の合計開口面積は、最上流の受熱器20で最も小さく、下流の受熱器11になるほど大きくなるように構成されている。これにより、帰還経路6側の下流の受熱器11内のドライアウトが抑制される。すなわち、冷却装置1は、過剰な量の液相の冷媒で受熱器11内を満たす必要が無く、薄い液相の冷媒の層を受熱器11内に形成することができ、高い冷却性能を有する。
As described above, the total opening area of the openings 38 of the return internal pipe 37 in each heat receiver 11 is configured to be the smallest in the most upstream heat receiver 20 and increase as the downstream heat receiver 11 is reached. Yes. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed. In other words, the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
また、各受熱器11における帰還内部管路37の開口部38の個数は、最上流の受熱器20で最も少なく、下流の受熱器11になるほど多くなる構成にしてもよい。これにより、最上流の受熱器20における帰還内部管路37の開口部38の個数が最も少ないので、最上流の受熱器20における帰還内部管路37の開口部38から液相の冷媒は流出しにくい。また、下流の受熱器11になるほど開口部38の個数が多くなるので、下流の受熱器11になるほど帰還内部管路37の開口部38から液相の冷媒は流出しやすくなる。これにより、下流の受熱器11において、ドライアウトが抑制される。
Further, the number of openings 38 of the return internal pipe 37 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may increase as the downstream heat receiver 11 is reached. As a result, the number of openings 38 of the return internal conduit 37 in the most upstream heat receiver 20 is the smallest, so that the liquid-phase refrigerant flows out from the opening 38 of the return internal conduit 37 in the most upstream heat receiver 20. Hateful. Further, since the number of the opening portions 38 increases as the downstream heat receiver 11 is reached, the liquid phase refrigerant is more likely to flow out from the opening portion 38 of the return internal pipe 37 as the downstream heat receiver 11 is formed. Thereby, in the downstream heat receiver 11, dryout is suppressed.
以上のようにして、各受熱器11における開口部38の個数は、最上流の受熱器20で最も少なく、下流の受熱器11になるほど多くなる構成にしてもよい。これにより、帰還経路6側の下流の受熱器11内のドライアウトが抑制される。すなわち、冷却装置1は、過剰な量の液相の冷媒で受熱器11内を満たす必要が無く、薄い液相の冷媒の層を受熱器11内に形成することができ、高い冷却性能を有する。
As described above, the number of openings 38 in each heat receiver 11 may be the smallest in the most upstream heat receiver 20 and may increase as the number of downstream heat receivers 11 increases. Thereby, the dryout in the downstream heat receiver 11 by the side of the return path 6 is suppressed. In other words, the cooling device 1 does not need to fill the heat receiver 11 with an excessive amount of liquid-phase refrigerant, can form a thin liquid-phase refrigerant layer in the heat receiver 11, and has high cooling performance. .
以上のように、本発明にかかる冷却装置は、冷却性能が高いので、中央演算処理装置(CPU)、大規模集積回路(LSI)、絶縁ゲートバイポーラトランジスタ(IGBT)、ダイオード等の電子部品を冷却する冷却装置として有用である。
As described above, since the cooling device according to the present invention has high cooling performance, it cools electronic components such as a central processing unit (CPU), a large scale integrated circuit (LSI), an insulated gate bipolar transistor (IGBT), and a diode. It is useful as a cooling device.
1 冷却装置
2 フィン部
3 受熱部
4 放熱部
5 放熱経路
6 帰還経路
7 冷却水供給経路
8 冷却水戻り経路
11 受熱器
15 第1の受熱板
16 第2の受熱板
19 固定用ネジ孔
20 最上流の受熱器
21 最下流の受熱器
22 第1のフィン
23 第2のフィン
24 帰還内部経路
25 放熱内部経路
28 第1の発熱体群
29 第2の発熱体群
30 流入口
31 流出口
32 仕切板
33 開口部
34 仕切壁
35 放熱内部経路開口
36 帰還内部経路開口
37 帰還内部管路
38 開口部
43 第1の発熱体
44 第2の発熱体
45 第3の発熱体
50 電子機器
51 ケース DESCRIPTION OFSYMBOLS 1 Cooling device 2 Fin part 3 Heat receiving part 4 Heat radiating part 5 Heat radiating path 6 Return path 7 Cooling water supply path 8 Cooling water return path 11 Heat receiver 15 1st heat receiving plate 16 2nd heat receiving plate 19 Fixing screw hole 20 Maximum Upper heat receiver 21 Most downstream heat receiver 22 First fin 23 Second fin 24 Return internal path 25 Radiation internal path 28 First heating element group 29 Second heating element group 30 Inlet 31 Outlet 32 Partition Plate 33 Opening 34 Partition wall 35 Heat dissipation internal path opening 36 Return internal path opening 37 Return internal conduit 38 Opening 43 First heating element 44 Second heating element 45 Third heating element 50 Electronic device 51 Case
2 フィン部
3 受熱部
4 放熱部
5 放熱経路
6 帰還経路
7 冷却水供給経路
8 冷却水戻り経路
11 受熱器
15 第1の受熱板
16 第2の受熱板
19 固定用ネジ孔
20 最上流の受熱器
21 最下流の受熱器
22 第1のフィン
23 第2のフィン
24 帰還内部経路
25 放熱内部経路
28 第1の発熱体群
29 第2の発熱体群
30 流入口
31 流出口
32 仕切板
33 開口部
34 仕切壁
35 放熱内部経路開口
36 帰還内部経路開口
37 帰還内部管路
38 開口部
43 第1の発熱体
44 第2の発熱体
45 第3の発熱体
50 電子機器
51 ケース DESCRIPTION OF
Claims (9)
- 冷媒の相変化によって発熱体を冷却する冷却装置において、
受熱部、放熱経路、放熱部および帰還経路を順に連結して形成される前記冷媒の循環経路を備え、
前記受熱部は、
前面および後面が最大面積の横長の直方体形状であり、
前記前面または前記後面の少なくとも一方に複数の前記発熱体が設置される受熱板と、
前記受熱部の上部に設けられ、前記冷媒が流通する放熱内部経路と、
前記受熱部の下部に設けられ、前記冷媒が流通する帰還内部経路と、
前記放熱内部経路と前記帰還内部経路との間に設けられ、複数の平板状のフィンを有するフィン部と、
前記放熱経路と前記放熱内部経路とを接続する流出口と、
前記帰還経路と前記帰還内部経路とを接続する流入口と、
前記受熱部の前記前面と前記後面との間に、前記フィンと平行方向になるように設けられる1または複数の仕切壁と、
前記仕切壁と前記受熱部の内壁とで囲まれて形成される複数の受熱器と、
前記仕切壁において、各前記受熱器の前記放熱内部経路を連通させる放熱内部経路開口と、
前記仕切壁において、各前記受熱器の前記帰還内部経路を連通させる帰還内部経路開口とを備え、
前記流入口と前記流出口とは、前記受熱部の同一の側面に設けられ、
前記フィンは、前記受熱板から内部に突出し、前記フィン間の隙間により構成される前記冷媒の流路が上下方向となるように設けられ、
前記帰還経路側の最下流の前記受熱器に前記受熱板を介して設置された前記発熱体の発熱量は、上流の前記受熱器に前記受熱板を介して設置された前記発熱体の発熱量よりも小さい冷却装置。 In the cooling device that cools the heating element by the phase change of the refrigerant,
A circulation path for the refrigerant formed by sequentially connecting a heat receiving section, a heat radiation path, a heat radiation section, and a return path;
The heat receiving part is
The front and back are horizontally long rectangular parallelepiped shapes with the largest area,
A heat receiving plate in which a plurality of the heating elements are installed on at least one of the front surface or the rear surface;
A heat dissipating internal path through which the refrigerant flows, provided above the heat receiving portion;
A return internal path that is provided at a lower portion of the heat receiving section and through which the refrigerant flows;
A fin portion provided between the heat dissipation internal path and the return internal path, and having a plurality of plate-like fins;
An outlet that connects the heat dissipation path and the heat dissipation internal path;
An inlet connecting the return path and the return internal path;
One or more partition walls provided between the front surface and the rear surface of the heat receiving portion so as to be parallel to the fins;
A plurality of heat receivers formed by being surrounded by the partition wall and the inner wall of the heat receiving unit;
In the partition wall, a heat dissipation internal path opening for communicating the heat dissipation internal path of each of the heat receivers,
A return internal path opening for communicating the return internal path of each of the heat receivers in the partition wall;
The inflow port and the outflow port are provided on the same side surface of the heat receiving unit,
The fin protrudes from the heat receiving plate and is provided so that a flow path of the refrigerant formed by a gap between the fins is in the vertical direction.
The amount of heat generated by the heating element installed in the most downstream heat receiving device on the return path side via the heat receiving plate is the amount of heat generated by the heating element installed in the upstream heat receiving device via the heat receiving plate. Smaller cooling device. - 前記受熱部は、
前記帰還内部経路と前記フィン部との間に、前記受熱部の底面と平行になるように設けられた仕切板を備え、
前記仕切板は、複数の開口部を有する請求項1に記載の冷却装置。 The heat receiving part is
A partition plate provided between the return internal path and the fin portion so as to be parallel to the bottom surface of the heat receiving portion,
The cooling device according to claim 1, wherein the partition plate has a plurality of openings. - 前記受熱部は、
前記帰還内部経路に設けられ、前記冷媒が流通する帰還内部管路を備え、
前記帰還内部経路開口は、前記仕切壁において、各前記受熱器の前記帰還内部管路を連通させ、
前記帰還内部管路は、複数の開口部を有する請求項1に記載の冷却装置。 The heat receiving part is
Provided in the return internal path, comprising a return internal conduit through which the refrigerant flows,
The return internal path opening communicates the return internal pipe line of each of the heat receivers in the partition wall,
The cooling device according to claim 1, wherein the return internal conduit has a plurality of openings. - 各前記受熱器における前記仕切板の前記開口部の合計開口面積は、最上流の前記受熱器で最も小さく、下流の前記受熱器になるほど大きくなる請求項2に記載の冷却装置。 The cooling device according to claim 2, wherein a total opening area of the openings of the partition plates in each of the heat receivers is the smallest in the most upstream heat receiver and increases as the downstream heat receiver is reached.
- 各前記受熱器における前記帰還内部管路の前記開口部の合計開口面積は、最上流の前記受熱器で最も小さく、下流の前記受熱器になるほど大きくなる請求項3に記載の冷却装置。 4. The cooling device according to claim 3, wherein a total opening area of the openings of the return internal pipe line in each of the heat receivers is the smallest in the most upstream heat receiver and becomes larger as the downstream heat receiver becomes.
- 各前記受熱器における前記仕切板の前記開口部の個数は、最上流の前記受熱器で最も少なく、下流の前記受熱器になるほど多くなる請求項2に記載の冷却装置。 The cooling device according to claim 2, wherein the number of the openings of the partition plate in each of the heat receivers is the smallest in the most upstream heat receiver and increases as the downstream heat receiver becomes.
- 各前記受熱器における前記帰還内部管路の前記開口部の個数は、最上流の前記受熱器で最も少なく、下流の前記受熱器になるほど多くなる請求項3に記載の冷却装置。 4. The cooling device according to claim 3, wherein the number of the openings of the return internal pipe line in each of the heat receivers is the smallest in the most upstream heat receiver and increases as the downstream heat receiver is increased.
- 前記発熱体は、前記受熱部の底面から距離を置いて前記受熱板に設置される請求項1に記載の冷却装置。 The cooling device according to claim 1, wherein the heating element is installed on the heat receiving plate at a distance from a bottom surface of the heat receiving unit.
- 請求項1に記載の冷却装置を搭載した電子機器。 An electronic device equipped with the cooling device according to claim 1.
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