US20200072565A1 - Thermal transfer device having a fluid conduit - Google Patents
Thermal transfer device having a fluid conduit Download PDFInfo
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- US20200072565A1 US20200072565A1 US16/546,785 US201916546785A US2020072565A1 US 20200072565 A1 US20200072565 A1 US 20200072565A1 US 201916546785 A US201916546785 A US 201916546785A US 2020072565 A1 US2020072565 A1 US 2020072565A1
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- Prior art keywords
- fluid conduit
- channels
- thermal transfer
- junction
- inlet
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
-
- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/03—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
- F28D1/0308—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
- F28D1/035—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other with U-flow or serpentine-flow inside the conduits
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- G—PHYSICS
- G06—COMPUTING OR CALCULATING; COUNTING
- G06F—ELECTRIC DIGITAL DATA PROCESSING
- G06F1/00—Details not covered by groups G06F3/00 - G06F13/00 and G06F21/00
- G06F1/16—Constructional details or arrangements
- G06F1/20—Cooling means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
- F28F13/08—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by varying the cross-section of the flow channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
- F28F13/12—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/12—Elements constructed in the shape of a hollow panel, e.g. with channels
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L23/00—Details of semiconductor or other solid state devices
- H01L23/34—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements
- H01L23/46—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements involving the transfer of heat by flowing fluids
- H01L23/473—Arrangements for cooling, heating, ventilating or temperature compensation ; Temperature sensing arrangements involving the transfer of heat by flowing fluids by flowing liquids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0028—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for cooling heat generating elements, e.g. for cooling electronic components or electric devices
- F28D2021/0029—Heat sinks
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2210/00—Heat exchange conduits
- F28F2210/02—Heat exchange conduits with particular branching, e.g. fractal conduit arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2210/00—Heat exchange conduits
- F28F2210/10—Particular layout, e.g. for uniform temperature distribution
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
- F28F2250/10—Particular pattern of flow of the heat exchange media
- F28F2250/102—Particular pattern of flow of the heat exchange media with change of flow direction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
- F28F2250/10—Particular pattern of flow of the heat exchange media
- F28F2250/108—Particular pattern of flow of the heat exchange media with combined cross flow and parallel flow
-
- G—PHYSICS
- G06—COMPUTING OR CALCULATING; COUNTING
- G06F—ELECTRIC DIGITAL DATA PROCESSING
- G06F2200/00—Indexing scheme relating to G06F1/04 - G06F1/32
- G06F2200/20—Indexing scheme relating to G06F1/20
- G06F2200/201—Cooling arrangements using cooling fluid
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K7/00—Constructional details common to different types of electric apparatus
- H05K7/20—Modifications to facilitate cooling, ventilating, or heating
- H05K7/20218—Modifications to facilitate cooling, ventilating, or heating using a liquid coolant without phase change in electronic enclosures
- H05K7/20254—Cold plates transferring heat from heat source to coolant
Definitions
- the present technology relates to thermal transfer devices having a fluid conduit.
- Heat dissipation is an important consideration for computer systems. Notably, many components of a computer system, such as a processor (also referred to as central processing unit (CPU)), generate heat and thus require cooling to avoid performance degradation and, in some cases, failure. Moreover, with advancing technological progress, processors are not only becoming more performant but also have a greater associated thermal design power (TDP) (i.e., a maximum amount of heat generated thereby which a cooling system should dissipate).
- TDP thermal design power
- heat sinks which rely on a heat transfer medium (e.g., a gas or liquid) to carry away the heat generated by a particular component of the computer system.
- a heat transfer medium e.g., a gas or liquid
- a water block which is a watercooling heat sink, is thermally coupled to the component to be cooled (e.g., the processor) and water is circulated through a conduit in the water block to absorb the heat from the component. As water flows out of the water block, so does the heat absorbed thereby.
- water blocks are susceptible to clogging and, in some cases, can be expensive to produce as manufacturing thereof can be time-consuming.
- the increasing cooling requirements of processors and other such components pose a challenge to water blocks.
- conventional water blocks are typically efficient only when operating with a relatively high water flow rate and at high pressure and thus require a pump system (for feeding water to the water block) with an accordingly high static head.
- a water block for cooling one of a central processing unit (CPU) and a graphics processing unit (GPU) of a computer system comprising:
- a body having a thermal transfer surface configured to be placed in contact with the one of the CPU and the GPU;
- a fluid conduit defined in the body and configured for conveying fluid through the body, the fluid conduit being thermally coupled to the thermal transfer surface, the fluid conduit having an inlet and an outlet, the fluid conduit being configured so that:
- a thermal transfer device includes a body having a thermal transfer surface configured to be placed in contact with a target component.
- the thermal transfer device also includes a fluid conduit defined in the body and configured for conveying fluid through the body.
- the fluid conduit is thermally coupled to the thermal transfer surface.
- the fluid conduit has an inlet and an outlet.
- the fluid conduit is configured so that: at a first junction, the fluid conduit branches into a first channel and a second channel which extend adjacent and generally parallel to one another along an initial portion of the fluid conduit; the first and second channels diverge away from one another at an end of the initial portion such that each of the first and second channels forms a serpentine path, the serpentine path formed by the first channel extending toward a first direction, the serpentine path formed by the second channel extending toward a second direction generally opposite to the first direction; and the first and second channels merge at a second junction.
- the first junction is the inlet of the fluid conduit.
- the second junction is the outlet of the fluid conduit.
- each of the first and second channels defines a sinusoidal pattern along at least a majority of a span thereof.
- a width of each of the first and second channels is constant.
- the width of each of first and second channels is between 1 mm and 4 mm inclusively.
- the serpentine path formed by each of the first and second channels defines a plurality of longitudinally-extending sections that are parallel to one another and laterally spaced from one another.
- the plurality of longitudinally-extending sections includes an innermost longitudinally-extending section that is closest to the first junction and an outermost longitudinally-extending section that is furthest from the first junction.
- the inlet is located centrally between the outermost longitudinally-extending section of the first channel and the outermost longitudinally-extending section of the second channel.
- the outlet is laterally aligned with the inlet.
- the first and second channels extend in opposite directions from the second junction.
- the body has a first body portion and a second body portion affixed to the first body portion.
- the fluid conduit is defined by the first and second body portions.
- a path of each of the first and second channels is defined by the first body portion.
- the inlet and the outlet are defined in the second body portion.
- the first and second body portions are welded to one another.
- the water block is generally rectangular.
- Embodiments of the present technology each have at least one of the above-mentioned object and/or aspects, but do not necessarily have all of them. It should be understood that some aspects of the present technology that have resulted from attempting to attain the above-mentioned object may not satisfy this object and/or may satisfy other objects not specifically recited herein.
- FIG. 1 is a perspective view of a thermal transfer device thermally coupled to a processor of a computer system
- FIG. 3 is top plan view of a base of the thermal transfer device of FIG. 1 , showing a fluid conduit thereof;
- FIG. 4 is a top plan view of the base of the thermal transfer device in accordance with another embodiment in which the fluid conduit is configured differently;
- FIG. 5 is a top plan view of the base of the thermal transfer device in accordance with another embodiment in which a path described by the fluid conduit is spiral;
- FIG. 6 is a perspective view of an embodiment of the thermal transfer device in which a cover of the thermal transfer device is screwed to the base;
- FIG. 7 is a top plan view of the base of the thermal transfer device in accordance with a variant of the embodiment of FIG. 4 ;
- FIG. 8 is a top plan view of the base of the thermal transfer device in accordance with another variant of the embodiment of FIG. 4 ;
- FIG. 9 is a top plan view of the base of the thermal transfer device in accordance with a variant of the embodiment of FIG. 5 .
- FIG. 1 illustrates a thermal transfer device 10 for cooling a target component 105 .
- the target component 105 is a central processing unit (CPU) of a computer system 100 and is mounted to a motherboard 102 thereof.
- the CPU 105 generates a significant amount of heat and, as is known, can benefit from cooling.
- the target component 105 could be any other suitable heat-generating component (e.g., a graphics processing unit (GPU)) or an intermediary component disposed between the thermal transfer device 10 and a heat-generating component.
- a graphics processing unit GPU
- the thermal transfer device 10 is a water block (i.e., a heat sink that uses water as a fluid medium for transferring heat) and will be referred to as such herein. It is nevertheless contemplated that a fluid other than water could be used in other embodiments.
- the water block 10 has a body 12 including two body portions 13 , 14 that are affixed to one another.
- the body portions 13 , 14 may be thought of as a cover 13 and a base 14 respectively.
- the body 12 (as well as each of the cover 13 and the base 14 thereof) is rectangular, with the cover 13 and the base 14 having identical lengths and widths such that, when the cover 13 is secured to the base 14 , as shown in FIG. 1 , the ends of the cover 13 and the base 14 are substantially flush with one another.
- the cover 13 and the base 14 are made of copper and are welded to one another. More specifically, the cover 13 is soldered onto the base 14 . In other embodiments, the cover 13 and the base 14 could be cold-welded or laser-welded together.
- the welding of the cover 13 and the base 14 prevents fluid leaks from the water block 10 without using any sealing members (e.g., a packing). Moreover, welding of the cover 13 and the base 14 allows using fewer elements such as screws or other fasteners for holding the cover 13 and the base 14 together.
- the water block 10 is thermally coupled to the CPU 105 for cooling thereof. More specifically, the body 12 has an external thermal transfer surface 20 (which is a lower surface of the base 14 ) that is placed in contact with the CPU 105 . As shown in FIG. 2 , the thermal transfer surface 20 is placed in contact with an upper surface of the CPU 105 to absorb heat therefrom. In some cases, a thermal paste may be disposed between the thermal transfer surface 20 and the CPU 105 , applied to the thermal transfer surface 20 or the upper surface of the CPU 105 , to improve heat transfer therebetween by ensuring continuity of contact between the thermal transfer surface 20 and the upper surface of the CPU 105 . Any other medium with adequate thermal conductivity for ensuring continuity of contact between the thermal transfer surface 20 and the upper surface of the CPU 105 may be used instead of the thermal paste in other cases.
- the fluid conduit 30 is thermally coupled to the thermal transfer surface 20 such that, when water flows in the fluid conduit 30 , heat absorbed by the thermal transfer surface 20 is subsequently absorbed by water flowing in the fluid conduit 30 .
- Water is received into the fluid conduit 30 via an inlet 32 and expelled therefrom via an outlet 34 .
- Both the inlet 32 and the outlet 34 are defined in the cover 13 (i.e., water enters and exits the body 12 via the cover 13 ).
- the inlet 32 is fluidly connected to a tube 16 through which water is fed into the fluid conduit 30 .
- a tube 18 is fluidly connected to the outlet 34 to discharge water from the fluid conduit 30 .
- the tubes 16 , 18 are copper tubes and are welded to the outer surface 22 of the body 12 (i.e., an outer surface of the cover 13 ).
- the fluid conduit 30 describes a path from the inlet 32 to the outlet 34 such as to guide the flow of water along the path. As will be described in greater detail below, the particular path described by the fluid conduit 30 may provide more efficient cooling of the CPU 105 .
- the path described by the fluid conduit 30 begins at the inlet 32 thereof which is laterally centered on the water block 10 . That is, as best seen in FIG. 3 , the inlet 32 is located centrally between the lateral ends of the water block 10 (and thus the lateral ends 29 , 31 of the base 14 ).
- the fluid conduit 30 branches into two channels 36 1 , 36 2 at the inlet 32 such that the flow of fluid within the fluid conduit 30 is split between both channels 36 1 , 36 2 . This may promote laminar flow of fluid within the fluid conduit 30 which reduces pressure drop of the fluid as it flows through the fluid conduit 30 .
- the channels 36 1 , 36 2 merge together again at the outlet 34 . However, in the span of the fluid conduit 30 between the inlet 32 and the outlet 34 , the channels 36 1 , 36 2 are fluidly separate from one another such that water flow from both channels 36 1 , 36 2 does not mix until reaching the outlet 34 .
- the path of the fluid conduit 30 (including the path of each of the channels 36 1 , 36 2 ) is defined by the base 14 independently of the cover 13 .
- the cover 13 defines part of the fluid conduit 30 (covering an open top thereof)
- the direction of the water flow within the fluid conduit 30 is defined by the recess 15 machined into the upper surface 24 of the base 14 .
- the cover 13 has a lower flat surface that closes the open top of the recess 15 (except at the inlet 32 and the outlet 34 ).
- the longitudinally-extending section 40 1 is an innermost one of the longitudinally-extending sections 40 1 - 40 7 (i.e., furthest away from the lateral end 31 ) and is part of the initial portion 38 .
- the longitudinally-extending section 40 7 is an outermost one of the longitudinally-extending sections 40 1 - 40 7 (i.e., closest to the lateral end 31 ).
- the channel 36 2 has a plurality of longitudinally-extending sections 42 1 - 42 7 that are parallel to one another, with adjacent ones of the longitudinally-extending sections 42 1 - 42 7 being connected by looping sections 46 1 - 46 6 .
- the longitudinally-extending section 42 1 is an innermost one of the longitudinally-extending sections 42 1 - 42 7 (i.e., furthest away from the lateral end 29 ) and part of the initial portion 38 .
- the longitudinally-extending section 42 7 is an outermost one of the longitudinally-extending sections 42 1 - 42 7 (i.e., closest to the lateral end 29 ).
- the longitudinally-extending sections 40 1 - 40 7 , 42 1 - 42 7 of the channels 36 1 , 36 2 have approximately the same length. This spreads the heat transfer capability more evenly throughout the thermal transfer surface 20 of the water block 10 .
- the innermost longitudinally-extending sections 40 1 , 42 1 of the channels 36 1 , 36 2 extend adjacent and parallel to one another along the initial portion 38 of the fluid conduit 30 .
- the innermost longitudinally-extending sections 40 1 , 42 1 are laterally aligned with the inlet 32 which, as mentioned above, is laterally centered between the lateral ends 29 , 31 of the base 14 (and thus the lateral ends of the water block 10 ).
- the inlet 32 is also located centrally between the outermost longitudinally-extending section 40 7 of the channel 36 1 and the outermost longitudinally-extending section 42 7 of the channel 36 2 .
- each of the channels 36 1 , 36 2 defines a sinusoidal pattern along a majority of a span thereof. That is, each one of the channels 36 1 , 36 2 has a repetitive pattern approximating that of a sinusoidal function along at least half of the span of that channel 36 1 , 36 2 .
- the sinusoidal pattern is defined along the longitudinally-extending portions 40 1 - 40 7 , 42 1 - 42 7 of the serpentine paths formed by the channels 36 1 , 36 2 .
- the sinusoidal pattern defined by the channels 36 1 , 36 2 changes a direction of the flow of water within the channels 36 1 , 36 2 as the flow of water engages the curves defined by the sinusoidal pattern.
- the channels 36 1 , 36 2 have a constant width (i.e., a distance between the opposite walls of each of the channels 36 1 , 36 2 is uniform along a span thereof) as the width is unaffected by the curves defined by the sinusoidal pattern.
- the width of each of the channels 36 1 , 36 2 is approximately 2 mm. In other embodiments, the width of each of the channels 36 1 , 36 2 may be between 1 mm and 4 mm inclusively.
- This relatively large width of the channels 36 1 , 36 2 allows using simple and fast manufacturing methods to produce the water block 10 in contrast with some conventional water blocks having “micro” channels made via electrical discharge machining.
- the channels 36 1 , 36 2 of the water block 10 can be machined (e.g., via a mill) with a tool having an adequate diameter. Therefore, this results in a more economic manufacturing process for producing the water block 10 .
- the relatively large width of the channels 36 1 , 36 2 may be helpful to restrict pressure drop of the water flow within the channels 36 1 , 36 2 , as well as to limit fouling of the channels 36 1 , 36 2 .
- the channels 36 1 , 36 2 may have any other suitable dimensions in other embodiments, so long as it is convenient for the flow regime within the channels 36 1 , 36 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
- a rotary cutter e.g., a mill or a router
- the channels 36 1 , 36 2 diverge to extend generally laterally (i.e., perpendicular to the outermost longitudinally-extending sections 40 7 , 42 7 ) toward one another and then merge at the outlet 34 .
- the channels 36 1 , 36 2 extend in opposite directions from the outlet 34 . It is noted that the outlet 34 is laterally aligned with the inlet 32 such that the outlet 34 is laterally centered between the ends 29 , 31 of the base 14 .
- the junction at which the two channels 36 1 , 36 2 merge could be at a location other than the outlet 34 .
- the two channels 36 1 , 36 2 could merge at a junction upstream from the outlet 34 (i.e., a location, along the path of the fluid conduit 30 , further from the outlet 34 ).
- the above-described configuration of the fluid conduit 30 allows routing relatively cool water to a target area 106 , as shown in FIG. 3 .
- the target area 106 corresponds to a hottest zone of the CPU 105 . That is, the target area 106 is an area of the water block 10 which, when the water block 10 is installed on the CPU 105 , overlies a point of the CPU 105 that exhibits a highest temperature during operation. As such, the target area 106 can benefit from being exposed to water that is as cool as possible.
- a distance along the fluid conduit 30 between the inlet 32 and the target area 106 is made relatively small since the inlet 32 is where water flowing within the fluid conduit 30 is coldest because heat has not yet substantially been transferred to the water.
- the inlet 32 is located centrally between the lateral ends 29 , 31 such as to be laterally aligned with the target area 106 and thus be relatively close thereto while at the same time allowing the fluid conduit 30 to overlap a majority of the area of the thermal transfer surface 20 .
- the initial portion 38 which is the portion of the fluid conduit 30 along which water flowing in the fluid conduit 30 is coldest due to its proximity to the inlet 32 , overlaps the target area 106 such as to bring the cool water from the inlet 32 to the target area 106 relatively quickly before the water absorbs a substantial amount of heat.
- the inlet and the outlet of the fluid conduit are located at opposite corners of the water block and thus the water travels a substantial distance (e.g., in a serpentine path) before it gets to the area corresponding to the hottest zone of the CPU or other component to be cooled.
- a substantial amount of heat has already been transferred to the water thus making it less efficient at absorbing heat from the hottest zone of the CPU.
- This configuration of the fluid conduit 30 allows the water block 10 to operate efficiently at a relatively low flow rate and low pressure, with limited pressure drop in the water flow.
- a pump needed for feeding the water block 10 can have a lower static head than if it were used for feeding a conventional water block that operates efficiently only at high flow rate and high pressure.
- the lower flow rate and pressure operating parameters of the water block 10 can allow a single pump to simultaneously feed multiple water blocks such as the water block 10 . This is particularly useful in cases where multiple components have to be cooled such as, for example, in a data center storing multiple servers that require cooling.
- the lower flow rate and pressure needed for efficient operation of the water block 10 can also carry over to the water circulation system to which the water block 10 is coupled.
- the water flow in the water circulation system is also subject to reduced pressure drop.
- the diameter of the tubing within which the water circulates in the water circulation system of the data center can also be reduced which, while causing an increase in the pressure drop in the water flow, results in a more compact water circulation system that is less costly and easier to install.
- a risk of leaks in the water circulation system is also reduced since the water circulation system is less pressurized.
- heat collected by the water blocks 10 leads to a temperature increase in the water circulation system which may be more convenient to design and operate the heat exchangers (e.g., chillers, dry coolers, plate heat exchangers) that are coupled to the water circulation system for releasing the heat collected by the water blocks 10 .
- this temperature increase in the water circulation system may lead to high outlet temperature, which may ease heat valorization (e.g. heating buildings in the winter).
- the water block 10 could operate at high inlet temperatures of up to 50° C., whereby water chillers for the water circulation system of the data center can be replaced by more preferable direct cooling solutions (e.g., dry coolers), which reduces costs and energy consumption associated with the implementation of water chillers.
- direct cooling solutions e.g., dry coolers
- the fluid conduit 30 of the above-described embodiment is replaced with a fluid conduit 130 .
- the path described by the fluid conduit 130 as defined by the base 14 is different from the fluid conduit 30 described above.
- the fluid conduit 130 is thermally coupled to the thermal transfer surface 20 such that, when water flows in the fluid conduit 130 , heat absorbed by the thermal transfer surface 20 is subsequently absorbed by water flowing in the fluid conduit 130 .
- Water is received into the fluid conduit 130 via an inlet 132 and expelled therefrom via an outlet 134 . Both the inlet 132 and the outlet 134 are defined in the cover 13 (i.e., water enters and exits the body 12 via the cover 13 ).
- the path described by the fluid conduit 130 begins at the inlet 132 thereof which is located generally at a corner of the rectangular water block 10 . That is, the inlet 132 is located adjacent an intersection of the longitudinal end 25 and the lateral end 31 of the base 14 .
- the fluid conduit 130 branches into two channels 136 1 , 136 2 at the inlet 32 such that the flow of fluid within the fluid conduit 130 is split between both channels 136 1 , 136 2 . As discussed above, this may promote laminar flow of fluid within the fluid conduit 130 which reduces pressure drop of the fluid as it flows through the fluid conduit 130 .
- the channels 136 1 , 136 2 extend parallel to one another along at least a majority of a span of the fluid conduit 130 .
- the channels 136 1 , 136 2 extend parallel and adjacent to one another from the inlet 132 to the outlet 134 . As will be described further below, the channels 136 1 , 136 2 merge together again at the outlet 134 . However, in the span of the fluid conduit 130 between the inlet 132 and the outlet 134 , the channels 136 1 , 136 2 are fluidly separate from one another such that water flow from both channels 136 1 , 136 2 does not mix until reaching the outlet 134 .
- the fluid conduit 130 could branch into more than two channels.
- the fluid conduit could branch into three channels or four channels.
- the junction at which the fluid conduit 130 branches into the two channels 136 1 , 136 2 could be at a location other than the inlet 132 .
- the fluid conduit 130 could branch into the two channels 136 1 , 136 2 at a junction downstream from the inlet 132 (i.e., a location, along the path of the fluid conduit 130 , further from the inlet 132 ).
- the junction at which the two channels 136 1 , 136 2 merge together could be upstream from the outlet 134 .
- the fluid conduit 130 forms a “serpentine” path.
- a serpentine path is herein defined as being a path that describes at least one S-shaped curve.
- the fluid conduit 130 defines a plurality of longitudinally-extending sections 140 1 - 140 7 that are parallel to one another and are laterally spaced from one another, with adjacent ones of the longitudinally-extending sections 140 1 - 140 7 being connected by looping sections 144 1 - 144 6 .
- the channels 136 1 , 136 2 of the fluid conduit 130 extend generally parallel to one another along the serpentine path (i.e., along the longitudinally-extending sections 140 1 - 140 7 and the looping sections 144 1 - 144 6 ).
- the inlet 132 is located at the longitudinally-extending section 140 1 and the outlet 134 is located at the longitudinally-extending section 140 7 such that the inlet 132 and the outlet 134 are located at the laterally furthest-most of the longitudinally-extending sections 140 1 - 140 7 respectively (i.e., the longitudinally-extending sections 140 1 - 140 7 which are most laterally spaced from one another).
- the inlet 132 and the outlet 134 are generally located at diagonally opposite corners of the rectangular water block 10 (like illustrated in FIG. 4 , with an even number of looping sections 144 1 - 144 6 ).
- the tubes 16 , 18 will be connected to the cover 13 at the corresponding diagonally opposite corners (unlike what is illustrated in FIG. 1 ) to be connected to the inlet 132 and the outlet 134 .
- the inlet 132 and the outlet 134 may be located at laterally opposite corners adjacent the same longitudinal end 25 . In such embodiments, the number of looping sections 144 x would be uneven (see looping sections 144 1 - 144 5 in FIG. 7 ).
- the two channels 136 1 , 136 2 could merge together at an intermediate junction between the inlet 132 and the outlet 134 , such that the fluid conduit 130 defines a single channel downstream of the intermediate junction before the fluid conduit 130 splits again into two channels 146 1 , 146 2 .
- the longitudinally-extending sections 140 1 - 140 3 are positioned, laterally, between the inlet 132 and an intermediate junction JCT 1 .
- the two channels 136 1 , 136 2 extend along each of the longitudinally-extending sections 140 1 - 140 3 and looping sections 144 1 , 144 2 interconnecting the longitudinally-extending sections 140 1 - 140 3 .
- the two channels 136 1 , 136 2 merge into a single channel 155 which, alone, defines the path of the fluid conduit 130 from the intermediate junction JCT 1 to another intermediate junction JCT 2 downstream from the intermediate junction JCT 1 .
- the fluid conduit 130 defines a plurality of longitudinally-extending sections 145 1 - 145 3 that are parallel to one another and laterally spaced from one another, and extending between the intermediate junctions JCT 1 , JCT 2 .
- the single channel 155 extends along the longitudinally-extending sections 145 1 - 145 3 and the looping sections interconnecting the longitudinally-extending sections 145 1 - 145 3 .
- the longitudinally-extending sections 145 1 - 145 3 are substantially laterally centered between the lateral ends 29 , 31 and define a limited region of the fluid conduit 130 where heat transfer is prioritized over pressure drop. This may be beneficial for example in cases where heat generation of the CPU 105 is greatest at its center.
- the fluid conduit 130 again branches into two channels 146 1 , 146 2 at the intermediate junction JCT 2 downstream from the intermediate junction JCT 1 . Between the intermediate junction JCT 2 and the outlet 134 , the fluid conduit 130 defines longitudinally-extending sections 140 4 - 140 6 positioned parallel to one another and laterally spaced from one another, similarly to the previous longitudinally-extending sections 140 1 - 140 3 .
- the two channels 146 1 , 146 2 extend along each of the longitudinally-extending sections 140 4 - 140 6 and looping sections 144 3 , 144 4 interconnecting the longitudinally-extending sections 140 4 - 140 6 .
- the two channels 146 1 , 146 2 are configured similarly to the channels 136 1 , 136 2 —notably, the two channels 146 1 , 146 2 extend parallel to one another along at least a majority (i.e., a majority or an entirety) of a span thereof and each of the channels 146 1 , 146 2 also defines a sinusoidal pattern along at least a majority of a span thereof.
- the channels 146 1 , 146 2 merge at the outlet 134 downstream from the intermediate junction JCT 2 . As discussed above with regard to FIG.
- the outlet 134 is located at a diagonally opposite corner from the inlet 132 .
- the inlet 132 and the outlet 134 may be located at laterally opposite corners adjacent the same longitudinal end 25 , as discussed above with regard to FIG. 7 .
- Each of the channels 136 1 , 136 2 defines a sinusoidal pattern along a majority of a span thereof. That is, each one of the channels 136 1 , 136 2 has a repetitive pattern approximating that of a sinusoidal function along at least half of the span of that channel 136 1 , 136 2 .
- the sinusoidal pattern is defined along the longitudinally-extending portions 140 1 - 140 7 of the serpentine path of the fluid conduit 130 .
- the sinusoidal pattern defined by the channels 136 1 , 136 2 changes a direction of the flow of water within the channels 136 1 , 136 2 as the flow of water engages the curves defined by the sinusoidal pattern.
- the channels 136 1 , 136 2 have a constant width (i.e., a distance between the opposite walls of each of the channels 136 1 , 136 2 is uniform along a span thereof) as the width is unaffected by the curves defined by the sinusoidal pattern.
- the width of each of the channels 136 1 , 136 2 is 2 mm.
- the width of the channels of each of the channels 136 1 , 136 2 may be between 1 mm and 4 mm.
- the channels 136 1 , 136 2 may have any other suitable dimensions in other embodiments so long as it is convenient for the flow regime within the channels 136 1 , 136 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
- a rotary cutter e.g., a mill or a router
- the fluid conduit 130 is defined by the cover 13 and the base 14 when the cover 13 and the base 14 are affixed to one another.
- the path of the fluid conduit 130 (including the path of each of the channels 136 1 , 136 2 ) is defined by the base 14 independently of the cover 13 .
- the cover 13 defines part of the fluid conduit 130 (covering an open top thereof)
- the direction of the water flow within the fluid conduit 30 is defined by the recess 115 machined into the upper surface 24 of the base 14 .
- the cover 13 has a lower flat surface that closes the open top of the recess 115 (except at the inlet 132 and the outlet 134 ).
- the fluid conduit 30 is replaced with a fluid conduit 230 .
- the path described by the fluid conduit 230 as defined by the base 14 is different from the fluid conduits 30 , 130 described above.
- the fluid conduit 230 is thermally coupled to the thermal transfer surface 20 such that, when water flows in the fluid conduit 230 , heat absorbed by the thermal transfer surface 20 is subsequently absorbed by water flowing in the fluid conduit 230 .
- Water is received into the fluid conduit 230 via an inlet 232 and expelled therefrom via an outlet 234 . Both the inlet 232 and the outlet 234 are defined in the cover 13 (i.e., water enters and exits the body 12 via the cover 13 ).
- the fluid conduit 230 branches into two channels 236 1 , 236 2 at the inlet 232 such that the flow of fluid within the fluid conduit 230 is split between both channels 236 1 , 236 2 . As discussed above, this may promote laminar flow of fluid within the fluid conduit 230 which reduces pressure drop of the fluid as it flows therethrough.
- the channels 236 1 , 236 2 extend parallel to one another along at least a majority of a span of the fluid conduit 230 . More specifically, in this embodiment, the channels 236 1 , 236 2 extend parallel from the inlet 232 to the outlet 234 . As will be described further below, the channels 236 1 , 236 2 merge together again at the outlet 234 .
- the channels 236 1 , 236 2 are fluidly separate from one another such that water flow from both channels 236 1 , 236 2 does not mix until reaching the outlet 234 .
- the fluid conduit 230 could branch into more than two channels.
- the fluid conduit could branch into three channels or four channels.
- the junction at which the fluid conduit 230 branches into the two channels 236 1 , 236 2 could be at a location other than the inlet 232 .
- the fluid conduit 230 could branch into the two channels 236 1 , 236 2 at a junction JCT downstream from the inlet 232 (i.e., a location, along the path of the fluid conduit 230 , further from the inlet 232 ).
- This configuration may be advantageous to prioritize heat transfer at a given region of the fluid conduit 230 . For instance, in such a configuration as that depicted in FIG.
- heat transfer in the region from the inlet 232 to the junction JCT may be greater than in the remainder of the fluid conduit 230 while incurring some pressure drop in the water in this limited region of the fluid conduit 230 (since the water flow is not split into the two channels 236 1 , 236 2 in this region).
- the junction at which the two channels 236 1 , 236 2 merge together could be upstream from the outlet 234 .
- Each of the channels 236 1 , 236 2 has a constant width (i.e., a distance between the opposite walls of each of the channels 236 1 , 236 2 is uniform along a span thereof).
- the width of each of the channels 236 1 , 236 2 is 2 mm.
- the width of the channels of each of the channels 236 1 , 236 2 may be between 1 mm and 4 mm.
- the channels 236 1 , 236 2 may have any other suitable dimensions in other embodiments, so long as it is convenient for the flow regime within the channels 236 1 , 236 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
- the fluid conduit 230 forms a generally rectangular spiral path centered about the inlet 232 . More specifically, the path of the fluid conduit 230 begins at the inlet 232 and extends further away from the inlet 232 as it revolves around the inlet 232 .
- the spiral path of the fluid conduit 230 ends at the outlet 234 which is positioned at an outer periphery of the spiral path formed by the fluid conduit 230 .
- the spiral path of the fluid conduit 230 is formed by ring sections 250 1 - 250 5 of the fluid conduit 230 .
- the ring sections 250 1 - 250 5 are concentric about the inlet 232 .
- the innermost ring section 250 1 is closest to the inlet 232 and the outermost ring section 250 5 is furthest form the inlet 232 .
- the outlet 234 is located at the outermost ring section 250 5 . Since the outlet 234 is located generally at a corner of the rectangular water block 10 , the spiral path of the fluid conduit 230 spreads across almost an entirety of the area of the water block 10 (i.e., the recess 215 in the upper surface 24 of the base 14 spans most of a length and a width of the base 14 ).
- the rectangular spiral path of the fluid conduit 230 is generally square (i.e., the length and width of the fluid conduit 230 are approximately similar). However, in some cases, the length of the spiral path of the fluid conduit 230 be greater than its width. This may better accommodate the rectangular shape of the CPU 105 (or other component to be cooled).
- the spiral path of the fluid conduit 230 does not include many tight curves (i.e., the radius of curvature of most if not all curves is relatively large) which facilitates and speeds up machining of the recess 215 in the base 14 .
- the radius of curvature of the curves of the spiral path may increase in proportion to a distance of the curve relative to the inlet 232 . That is, the further from the central inlet 232 a curve of the spiral path is, the greater its radius of curvature.
- the fluid conduit 230 is defined by the cover 13 and the base 14 when the cover 13 and the base 14 are affixed to one another.
- the path of the fluid conduit 230 (including the path of each of the channels 236 1 , 236 2 ) is defined by the base 14 independently of the cover 13 .
- the cover 13 defines part of the fluid conduit 230 (covering an open top thereof)
- the direction of the water flow within the fluid conduit 230 is defined by the recess 215 machined into the upper surface 24 of the base 14 .
- the cover 13 has a lower flat surface that closes the open top of the recess 215 (except at the inlet 132 and the outlet 134 ).
- the cover and base may be affixed to one another differently.
- a cover 13 ′ and a base 14 ′ are affixed to one another by fasteners 19 (e.g., screws).
- the cover 13 ′ has holes extending therethrough for receiving the fasteners 19
- the base 14 ′ has corresponding receiving openings (not shown) that are threaded to receive the fasteners 19 .
- a sealing member e.g., a gasket
- the cover 13 ′ is made of a polymeric material (the base 14 ′ is still made of copper).
- the cover 13 ′ may be an injection molded component.
- the tubes 16 , 18 are also made of polymeric material. A resin may seal the interface between the tubes 16 , 18 and the cover 13 ′.
- thermal transfer device 10 has been described above as being configured for absorbing heat from the target component 105 , it is contemplated that, in alternative embodiments, the thermal transfer device 10 could be used for transferring heat to the target component 105 (in such a case, the target component is not a CPU).
- thermal transfer device 10 implemented in accordance with some non-limiting embodiments of the present technology can be represented as presented in the following numbered clauses.
- CLAUSE 3 The thermal transfer device of clause 1 or 2, wherein the second junction is the outlet ( 234 ) of the fluid conduit ( 230 ).
- CLAUSE 4 The thermal transfer device of any one of clauses 1 to 3, wherein the spiral path is a generally square spiral path.
- CLAUSE 5 The thermal transfer device of any one of clauses 1 to 4, wherein the outlet ( 234 ) is positioned at an outer periphery of the spiral path formed by fluid conduit ( 230 ).
- CLAUSE 6 The thermal transfer device of any one of clauses 1 to 5, wherein a width of each of the at least two channels ( 236 1 , 236 2 ) is constant.
- CLAUSE 7 The thermal transfer device of clause 6, wherein the width of each of the at least two channels ( 236 1 , 236 2 ) is between 1 mm and 4 mm inclusively.
- CLAUSE 8 The thermal transfer device of any one of clauses 1 to 7, wherein: the body ( 12 ) comprises a first body portion ( 14 ) and a second body portion ( 13 ) affixed to the first body portion ( 14 ); the fluid conduit ( 230 ) is defined by the first and second body portions ( 14 , 13 ); and a path of each of the at least two channels ( 236 1 , 236 2 ) is defined by the first body portion ( 14 ).
- CLAUSE 9 The thermal transfer device of clause 8, wherein the inlet ( 232 ) and the outlet ( 234 ) are defined in the second body portion ( 13 ).
- CLAUSE 10 The thermal transfer device of clause 8, wherein the first and second body portions ( 14 , 13 ) are welded to one another.
- CLAUSE 14 The thermal transfer device of clause 13, wherein the first junction is the inlet ( 132 ) of the fluid conduit ( 130 ).
- CLAUSE 15 The thermal transfer device of clause 13 or 14, wherein the second junction is the outlet ( 134 ) of the fluid conduit ( 130 ).
- the serpentine path formed by the fluid conduit ( 130 ) defines a plurality of longitudinally-extending sections ( 140 1 - 140 7 ) that are parallel to one another and laterally spaced from one another;
- the plurality of longitudinally-extending sections ( 140 1 - 140 7 ) includes a first longitudinally-extending section ( 140 1 ) and a second longitudinally-extending section ( 140 7 ) that are laterally furthest-most of the longitudinally-extending sections ( 140 1 - 140 7 ); the first junction is located at the first longitudinally-extending section ( 140 1 ); and the second junction is located at the second longitudinally-extending section ( 140 7 ).
- CLAUSE 17 The thermal transfer device of any one of clauses 13 to 16, wherein a width of each of the at least two channels ( 136 1 , 136 2 ) is constant.
- CLAUSE 18 The thermal transfer device of clause 17, wherein the width of each of the at least two channels ( 136 1 , 136 2 ) is between 1 mm and 4 mm inclusively.
- the second junction is a first intermediate junction (JCT 1 ) downstream from the first junction; the fluid conduit ( 130 ) branches into an other at least two channels ( 146 1 , 146 2 ) at a second intermediate junction (JCT 2 ) between the first intermediate junction (JCT 1 ) and the outlet ( 134 ); between the first and second intermediate junctions (JCT 1 , JCT 2 ), the fluid conduit ( 130 ) defines a plurality of longitudinally-extending sections ( 145 1 - 145 3 ) that are parallel to one another and laterally spaced from one another, the fluid conduit ( 130 ) having a single channel ( 155 ) extending along the longitudinally-extending sections ( 145 1 - 145 3 ); the longitudinally-extending sections ( 145 1 - 145 3 ) are substantially laterally centered between lateral ends of the body ( 12 ); the other at least two channels ( 146 1 , 146 2 ) merge at a fourth junction.
- JCT 1 first intermediate junction
- JCT 2 second intermediate junction
- each of the other at least two channels ( 146 1 , 146 2 ) defines a sinusoidal pattern along at least a majority of a span thereof.
- CLAUSE 21 The thermal transfer device of any one of clauses 13 to 20, wherein the serpentine path of the fluid conduit ( 130 ) extends from the inlet ( 132 ) to the outlet ( 134 ).
- CLAUSE 22 The thermal transfer device of any one of clauses 13 to 19, wherein: the body ( 12 ) comprises a first body portion ( 14 ) and a second body portion ( 13 ) affixed to the first body portion ( 14 ); the fluid conduit ( 130 ) is defined by the first and second body portions ( 14 , 13 ); and a path of each of the at least two channels ( 136 1 , 136 2 ) is defined by the first body portion ( 14 ).
- CLAUSE 23 The thermal transfer device of clause 22, wherein the inlet ( 132 ) and the outlet ( 134 ) are defined in the second body portion ( 13 ).
- CLAUSE 24 The thermal transfer device of clause 22, wherein the first and second body portions ( 14 , 13 ) are welded to one another.
- CLAUSE 25 The thermal transfer device of any one of clauses 13 to 22 being a water block.
- CLAUSE 26 The thermal transfer device of clause 25, wherein the water block is generally rectangular.
- CLAUSE 27 The thermal transfer device of clause 26, wherein the inlet ( 132 ) and the outlet ( 134 ) are generally located at diagonally opposite corners of the rectangular water block.
- CLAUSE 28 The thermal transfer device of clause 26, wherein the inlet ( 132 ) and the outlet ( 134 ) are generally located at laterally opposite corners of the rectangular water block.
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Abstract
A thermal transfer device has a body and a fluid conduit defined in the body. The body has a thermal transfer surface configured to be placed in contact with a target component. The fluid conduit is configured for conveying fluid through the body and is thermally coupled to the thermal transfer surface. The fluid conduit is configured so that: at a first junction, the fluid conduit branches into a first channel and a second channel which extend adjacent and generally parallel to one another along an initial portion of the fluid conduit; the first and second channels diverge away from one another at an end of the initial portion such that each of the first and second channels forms a serpentine path; and the first and second channels merge at a second junction. The serpentine paths formed by the first and second channels extend toward generally opposite directions.
Description
- The present application claims priority from European Patent Application No. 1 831 5027.5 filed on Sep. 4, 2018, the entirety of which is incorporated herein by reference.
- The present technology relates to thermal transfer devices having a fluid conduit.
- Heat dissipation is an important consideration for computer systems. Notably, many components of a computer system, such as a processor (also referred to as central processing unit (CPU)), generate heat and thus require cooling to avoid performance degradation and, in some cases, failure. Moreover, with advancing technological progress, processors are not only becoming more performant but also have a greater associated thermal design power (TDP) (i.e., a maximum amount of heat generated thereby which a cooling system should dissipate).
- Many solutions exist for promoting heat dissipation in computer systems. Amongst them are heat sinks which rely on a heat transfer medium (e.g., a gas or liquid) to carry away the heat generated by a particular component of the computer system. For instance, a water block, which is a watercooling heat sink, is thermally coupled to the component to be cooled (e.g., the processor) and water is circulated through a conduit in the water block to absorb the heat from the component. As water flows out of the water block, so does the heat absorbed thereby.
- However, water blocks are susceptible to clogging and, in some cases, can be expensive to produce as manufacturing thereof can be time-consuming. In addition, the increasing cooling requirements of processors and other such components pose a challenge to water blocks. Moreover, conventional water blocks are typically efficient only when operating with a relatively high water flow rate and at high pressure and thus require a pump system (for feeding water to the water block) with an accordingly high static head.
- There is therefore a desire for a thermal transfer device which can alleviate at least some of these drawbacks.
- It is an object of the present technology to ameliorate at least some of the inconveniences present in the prior art.
- According to one aspect of the present technology, there is provided a water block for cooling one of a central processing unit (CPU) and a graphics processing unit (GPU) of a computer system, the water block comprising:
- a body having a thermal transfer surface configured to be placed in contact with the one of the CPU and the GPU;
- a fluid conduit defined in the body and configured for conveying fluid through the body, the fluid conduit being thermally coupled to the thermal transfer surface, the fluid conduit having an inlet and an outlet, the fluid conduit being configured so that:
-
- at a first junction, the fluid conduit branches into a first channel and a second channel which extend adjacent and generally parallel to one another along an initial portion of the fluid conduit;
- the first and second channels diverge away from one another at an end of the initial portion such that each of the first and second channels forms a serpentine path, the serpentine path formed by the first channel extending toward a first direction, the serpentine path formed by the second channel extending toward a second direction generally opposite to the first direction;
- the first and second channels merge at a second junction; and
- each of the first and second channels defines a sinusoidal pattern along at least a majority of a span thereof.
- According to another aspect of the present technology, there is provided a thermal transfer device. The thermal transfer device includes a body having a thermal transfer surface configured to be placed in contact with a target component. The thermal transfer device also includes a fluid conduit defined in the body and configured for conveying fluid through the body. The fluid conduit is thermally coupled to the thermal transfer surface. The fluid conduit has an inlet and an outlet. The fluid conduit is configured so that: at a first junction, the fluid conduit branches into a first channel and a second channel which extend adjacent and generally parallel to one another along an initial portion of the fluid conduit; the first and second channels diverge away from one another at an end of the initial portion such that each of the first and second channels forms a serpentine path, the serpentine path formed by the first channel extending toward a first direction, the serpentine path formed by the second channel extending toward a second direction generally opposite to the first direction; and the first and second channels merge at a second junction.
- In some embodiments, the first junction is the inlet of the fluid conduit.
- In some embodiments, the second junction is the outlet of the fluid conduit.
- In some embodiments, each of the first and second channels defines a sinusoidal pattern along at least a majority of a span thereof.
- In some embodiments, a width of each of the first and second channels is constant.
- In some embodiments, the width of each of first and second channels is between 1 mm and 4 mm inclusively.
- In some embodiments, the serpentine path formed by each of the first and second channels defines a plurality of longitudinally-extending sections that are parallel to one another and laterally spaced from one another.
- In some embodiments, the plurality of longitudinally-extending sections includes an innermost longitudinally-extending section that is closest to the first junction and an outermost longitudinally-extending section that is furthest from the first junction.
- In some embodiments, the inlet is located centrally between the outermost longitudinally-extending section of the first channel and the outermost longitudinally-extending section of the second channel.
- In some embodiments, the outlet is laterally aligned with the inlet.
- In some embodiments, the first and second channels extend in opposite directions from the second junction.
- In some embodiments, the body has a first body portion and a second body portion affixed to the first body portion. The fluid conduit is defined by the first and second body portions. A path of each of the first and second channels is defined by the first body portion.
- In some embodiments, the inlet and the outlet are defined in the second body portion.
- In some embodiments, the first and second body portions are welded to one another.
- In some embodiments, the thermal transfer device is a water block.
- In some embodiments, the water block is generally rectangular.
- Embodiments of the present technology each have at least one of the above-mentioned object and/or aspects, but do not necessarily have all of them. It should be understood that some aspects of the present technology that have resulted from attempting to attain the above-mentioned object may not satisfy this object and/or may satisfy other objects not specifically recited herein.
- Additional and/or alternative features, aspects and advantages of embodiments of the present technology will become apparent from the following description, the accompanying drawings and the appended claims.
- For a better understanding of the present technology, as well as other aspects and further features thereof, reference is made to the following description which is to be used in conjunction with the accompanying drawings, where:
-
FIG. 1 is a perspective view of a thermal transfer device thermally coupled to a processor of a computer system; -
FIG. 2 is a right side elevation view of the thermal transfer device ofFIG. 1 coupled to the processor; -
FIG. 3 is top plan view of a base of the thermal transfer device ofFIG. 1 , showing a fluid conduit thereof; -
FIG. 4 is a top plan view of the base of the thermal transfer device in accordance with another embodiment in which the fluid conduit is configured differently; -
FIG. 5 is a top plan view of the base of the thermal transfer device in accordance with another embodiment in which a path described by the fluid conduit is spiral; -
FIG. 6 is a perspective view of an embodiment of the thermal transfer device in which a cover of the thermal transfer device is screwed to the base; -
FIG. 7 is a top plan view of the base of the thermal transfer device in accordance with a variant of the embodiment ofFIG. 4 ; -
FIG. 8 is a top plan view of the base of the thermal transfer device in accordance with another variant of the embodiment ofFIG. 4 ; and -
FIG. 9 is a top plan view of the base of the thermal transfer device in accordance with a variant of the embodiment ofFIG. 5 . -
FIG. 1 illustrates athermal transfer device 10 for cooling atarget component 105. In this example, thetarget component 105 is a central processing unit (CPU) of acomputer system 100 and is mounted to amotherboard 102 thereof. In use, theCPU 105 generates a significant amount of heat and, as is known, can benefit from cooling. It is contemplated that thetarget component 105 could be any other suitable heat-generating component (e.g., a graphics processing unit (GPU)) or an intermediary component disposed between thethermal transfer device 10 and a heat-generating component. As will be described in detail below, in this embodiment, thethermal transfer device 10 is a water block (i.e., a heat sink that uses water as a fluid medium for transferring heat) and will be referred to as such herein. It is nevertheless contemplated that a fluid other than water could be used in other embodiments. - The
water block 10 has abody 12 including two 13, 14 that are affixed to one another. Thebody portions 13, 14 may be thought of as abody portions cover 13 and a base 14 respectively. The body 12 (as well as each of thecover 13 and thebase 14 thereof) is rectangular, with thecover 13 and the base 14 having identical lengths and widths such that, when thecover 13 is secured to thebase 14, as shown inFIG. 1 , the ends of thecover 13 and the base 14 are substantially flush with one another. In this embodiment, thecover 13 and the base 14 are made of copper and are welded to one another. More specifically, thecover 13 is soldered onto thebase 14. In other embodiments, thecover 13 and the base 14 could be cold-welded or laser-welded together. The welding of thecover 13 and thebase 14 prevents fluid leaks from thewater block 10 without using any sealing members (e.g., a packing). Moreover, welding of thecover 13 and thebase 14 allows using fewer elements such as screws or other fasteners for holding thecover 13 and the base 14 together. - The
water block 10 is thermally coupled to theCPU 105 for cooling thereof. More specifically, thebody 12 has an external thermal transfer surface 20 (which is a lower surface of the base 14) that is placed in contact with theCPU 105. As shown inFIG. 2 , thethermal transfer surface 20 is placed in contact with an upper surface of theCPU 105 to absorb heat therefrom. In some cases, a thermal paste may be disposed between thethermal transfer surface 20 and theCPU 105, applied to thethermal transfer surface 20 or the upper surface of theCPU 105, to improve heat transfer therebetween by ensuring continuity of contact between thethermal transfer surface 20 and the upper surface of theCPU 105. Any other medium with adequate thermal conductivity for ensuring continuity of contact between thethermal transfer surface 20 and the upper surface of theCPU 105 may be used instead of the thermal paste in other cases. - The
water block 10 has afluid conduit 30 defined in thebody 12 for conveying water therethrough. More specifically, thefluid conduit 30 is defined by surfaces of both thecover 13 and thebase 14. Notably, acontinuous recess 15 formed in theupper surface 24 of thebase 14 defines a path describes by thefluid conduit 30. - The
fluid conduit 30 is thermally coupled to thethermal transfer surface 20 such that, when water flows in thefluid conduit 30, heat absorbed by thethermal transfer surface 20 is subsequently absorbed by water flowing in thefluid conduit 30. Water is received into thefluid conduit 30 via aninlet 32 and expelled therefrom via anoutlet 34. Both theinlet 32 and theoutlet 34 are defined in the cover 13 (i.e., water enters and exits thebody 12 via the cover 13). As shown inFIGS. 1 and 2 , theinlet 32 is fluidly connected to atube 16 through which water is fed into thefluid conduit 30. Similarly, atube 18 is fluidly connected to theoutlet 34 to discharge water from thefluid conduit 30. In this embodiment, the 16, 18 are copper tubes and are welded to thetubes outer surface 22 of the body 12 (i.e., an outer surface of the cover 13). - The
fluid conduit 30 describes a path from theinlet 32 to theoutlet 34 such as to guide the flow of water along the path. As will be described in greater detail below, the particular path described by thefluid conduit 30 may provide more efficient cooling of theCPU 105. - The path described by the
fluid conduit 30 begins at theinlet 32 thereof which is laterally centered on thewater block 10. That is, as best seen inFIG. 3 , theinlet 32 is located centrally between the lateral ends of the water block 10 (and thus the lateral ends 29, 31 of the base 14). Thefluid conduit 30 branches into two channels 36 1, 36 2 at theinlet 32 such that the flow of fluid within thefluid conduit 30 is split between both channels 36 1, 36 2. This may promote laminar flow of fluid within thefluid conduit 30 which reduces pressure drop of the fluid as it flows through thefluid conduit 30. As will be described further below, the channels 36 1, 36 2 merge together again at theoutlet 34. However, in the span of thefluid conduit 30 between theinlet 32 and theoutlet 34, the channels 36 1, 36 2 are fluidly separate from one another such that water flow from both channels 36 1, 36 2 does not mix until reaching theoutlet 34. - It is contemplated that, in alternative embodiments, the junction at which the
fluid conduit 30 branches into the two channels 36 1, 36 2 could be at a location other than theinlet 32. For example, thefluid conduit 30 could branch into the two channels 36 1, 36 2 at a junction downstream from the inlet 32 (i.e., a location, along the path of thefluid conduit 30, further from the inlet 32). Similarly, it is contemplated that, in alternative embodiments, the junction at which the two channels 36 1, 36 2 merge together could be upstream from theoutlet 34. - In this embodiment, the path of the fluid conduit 30 (including the path of each of the channels 36 1, 36 2) is defined by the base 14 independently of the
cover 13. In other words, while thecover 13 defines part of the fluid conduit 30 (covering an open top thereof), the direction of the water flow within thefluid conduit 30 is defined by therecess 15 machined into theupper surface 24 of thebase 14. For its part, thecover 13 has a lower flat surface that closes the open top of the recess 15 (except at theinlet 32 and the outlet 34). - The channels 36 1, 36 2 extend adjacent and parallel to one another along an
initial portion 38 of thefluid conduit 30 beginning at the junction at which the channels 36 1, 36 2 begin (i.e., at theinlet 32 in this embodiment). Theinitial portion 38 is the portion of thefluid conduit 30 along which the channels 36 1, 36 2 are closest to one another aside from when the channels 36 1, 36 2 merge again at theoutlet 34. At an end of theinitial portion 38, the channels 36 1, 36 2 diverge from one another such that each of the channels 36 1, 36 2 forms a “serpentine” path. The serpentine paths of the channels 36 1, 36 2 extend toward generally opposite lateral directions (i.e., one extends toward thelateral end 29 while the other extends toward the opposite lateral end 31). A serpentine path is herein defined as being a path that describes at least one S-shaped curve. More specifically, the serpentine path formed by each of the channels 36 1, 36 2 includes a plurality of longitudinally-extending sections that extend generally longitudinally and which are connected by looping sections. For instance, the channel 36 1 has a plurality of longitudinally-extending sections 40 1-40 7 that are parallel to one another and are laterally spaced from one another, with adjacent ones of the longitudinally-extending sections 40 1-40 7 being connected by looping sections 44 1-44 6. The longitudinally-extending section 40 1 is an innermost one of the longitudinally-extending sections 40 1-40 7 (i.e., furthest away from the lateral end 31) and is part of theinitial portion 38. The longitudinally-extending section 40 7 is an outermost one of the longitudinally-extending sections 40 1-40 7 (i.e., closest to the lateral end 31). - Similarly, the channel 36 2 has a plurality of longitudinally-extending sections 42 1-42 7 that are parallel to one another, with adjacent ones of the longitudinally-extending sections 42 1-42 7 being connected by looping sections 46 1-46 6. The longitudinally-extending section 42 1 is an innermost one of the longitudinally-extending sections 42 1-42 7 (i.e., furthest away from the lateral end 29) and part of the
initial portion 38. The longitudinally-extending section 42 7 is an outermost one of the longitudinally-extending sections 42 1-42 7 (i.e., closest to the lateral end 29). - As will be noted, the longitudinally-extending sections 40 1-40 7, 42 1-42 7 of the channels 36 1, 36 2 have approximately the same length. This spreads the heat transfer capability more evenly throughout the
thermal transfer surface 20 of thewater block 10. - The innermost longitudinally-extending sections 40 1, 42 1 of the channels 36 1, 36 2 extend adjacent and parallel to one another along the
initial portion 38 of thefluid conduit 30. As such, the innermost longitudinally-extending sections 40 1, 42 1 are laterally aligned with theinlet 32 which, as mentioned above, is laterally centered between the lateral ends 29, 31 of the base 14 (and thus the lateral ends of the water block 10). Theinlet 32 is also located centrally between the outermost longitudinally-extending section 40 7 of the channel 36 1 and the outermost longitudinally-extending section 42 7 of the channel 36 2. - In this embodiment, each of the channels 36 1, 36 2 defines a sinusoidal pattern along a majority of a span thereof. That is, each one of the channels 36 1, 36 2 has a repetitive pattern approximating that of a sinusoidal function along at least half of the span of that channel 36 1, 36 2. In this case, the sinusoidal pattern is defined along the longitudinally-extending portions 40 1-40 7, 42 1-42 7 of the serpentine paths formed by the channels 36 1, 36 2. The sinusoidal pattern defined by the channels 36 1, 36 2 changes a direction of the flow of water within the channels 36 1, 36 2 as the flow of water engages the curves defined by the sinusoidal pattern. Moreover, it is noted that the channels 36 1, 36 2 have a constant width (i.e., a distance between the opposite walls of each of the channels 36 1, 36 2 is uniform along a span thereof) as the width is unaffected by the curves defined by the sinusoidal pattern.
- In particular, in this embodiment, the width of each of the channels 36 1, 36 2 is approximately 2 mm. In other embodiments, the width of each of the channels 36 1, 36 2 may be between 1 mm and 4 mm inclusively. This relatively large width of the channels 36 1, 36 2 allows using simple and fast manufacturing methods to produce the
water block 10 in contrast with some conventional water blocks having “micro” channels made via electrical discharge machining. Notably, the channels 36 1, 36 2 of thewater block 10 can be machined (e.g., via a mill) with a tool having an adequate diameter. Therefore, this results in a more economic manufacturing process for producing thewater block 10. Moreover, the relatively large width of the channels 36 1, 36 2 may be helpful to restrict pressure drop of the water flow within the channels 36 1, 36 2, as well as to limit fouling of the channels 36 1, 36 2. - The channels 36 1, 36 2 may have any other suitable dimensions in other embodiments, so long as it is convenient for the flow regime within the channels 36 1, 36 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
- The sinusoidal pattern defined by the channels 36 1, 36 2 advantageously increases the contact area of the walls thereof compared to if the channels 36 1, 36 2 were linear (i.e., straight). This increased contact area results in improved heat transfer. The sinusoidal pattern also creates flow disturbances leading to greater friction between the water and the walls of the channels 36 1, 36 2 which also improves heat transfer therebetween and, moreover, limits the fouling rate and clogging within the channels 36 1, 36 2, while generating a limited increase of pressure drop compared to if the channels 36 1, 36 2 were linear.
- At the end of the outermost longitudinally-extending sections 40 7, 42 7 (i.e., the respective ends of the outermost longitudinally-extending sections 40 7, 42 7 closest, along the
fluid conduit 30, to the outlet 34), the channels 36 1, 36 2 diverge to extend generally laterally (i.e., perpendicular to the outermost longitudinally-extending sections 40 7, 42 7) toward one another and then merge at theoutlet 34. As such, the channels 36 1, 36 2 extend in opposite directions from theoutlet 34. It is noted that theoutlet 34 is laterally aligned with theinlet 32 such that theoutlet 34 is laterally centered between the 29, 31 of theends base 14. - It is contemplated that, in alternative embodiments, the junction at which the two channels 36 1, 36 2 merge could be at a location other than the
outlet 34. For example, the two channels 36 1, 36 2 could merge at a junction upstream from the outlet 34 (i.e., a location, along the path of thefluid conduit 30, further from the outlet 34). - The above-described configuration of the
fluid conduit 30 allows routing relatively cool water to atarget area 106, as shown inFIG. 3 . Thetarget area 106 corresponds to a hottest zone of theCPU 105. That is, thetarget area 106 is an area of thewater block 10 which, when thewater block 10 is installed on theCPU 105, overlies a point of theCPU 105 that exhibits a highest temperature during operation. As such, thetarget area 106 can benefit from being exposed to water that is as cool as possible. - To that end, a distance along the
fluid conduit 30 between theinlet 32 and thetarget area 106 is made relatively small since theinlet 32 is where water flowing within thefluid conduit 30 is coldest because heat has not yet substantially been transferred to the water. In particular, theinlet 32 is located centrally between the lateral ends 29, 31 such as to be laterally aligned with thetarget area 106 and thus be relatively close thereto while at the same time allowing thefluid conduit 30 to overlap a majority of the area of thethermal transfer surface 20. Theinitial portion 38, which is the portion of thefluid conduit 30 along which water flowing in thefluid conduit 30 is coldest due to its proximity to theinlet 32, overlaps thetarget area 106 such as to bring the cool water from theinlet 32 to thetarget area 106 relatively quickly before the water absorbs a substantial amount of heat. In contrast, in many conventional water block configurations, the inlet and the outlet of the fluid conduit are located at opposite corners of the water block and thus the water travels a substantial distance (e.g., in a serpentine path) before it gets to the area corresponding to the hottest zone of the CPU or other component to be cooled. As such, by the time the originally cool water gets to the area that corresponds to the hottest zone of the CPU, a substantial amount of heat has already been transferred to the water thus making it less efficient at absorbing heat from the hottest zone of the CPU. - This configuration of the
fluid conduit 30, and those described below with respect to other embodiments thereof, allows thewater block 10 to operate efficiently at a relatively low flow rate and low pressure, with limited pressure drop in the water flow. Moreover, due the lower flow rate and pressure operating parameters of thewater block 10, a pump needed for feeding thewater block 10 can have a lower static head than if it were used for feeding a conventional water block that operates efficiently only at high flow rate and high pressure. Alternatively or additionally, the lower flow rate and pressure operating parameters of thewater block 10 can allow a single pump to simultaneously feed multiple water blocks such as thewater block 10. This is particularly useful in cases where multiple components have to be cooled such as, for example, in a data center storing multiple servers that require cooling. - In addition, in an example of implementation such as a data center, the lower flow rate and pressure needed for efficient operation of the
water block 10 can also carry over to the water circulation system to which thewater block 10 is coupled. Thus, the water flow in the water circulation system is also subject to reduced pressure drop. Moreover, the diameter of the tubing within which the water circulates in the water circulation system of the data center can also be reduced which, while causing an increase in the pressure drop in the water flow, results in a more compact water circulation system that is less costly and easier to install. In addition, a risk of leaks in the water circulation system is also reduced since the water circulation system is less pressurized. Furthermore, due to the lower flow rate, heat collected by the water blocks 10 leads to a temperature increase in the water circulation system which may be more convenient to design and operate the heat exchangers (e.g., chillers, dry coolers, plate heat exchangers) that are coupled to the water circulation system for releasing the heat collected by the water blocks 10. Similarly, this temperature increase in the water circulation system may lead to high outlet temperature, which may ease heat valorization (e.g. heating buildings in the winter). Moreover, in some examples of implementation such as a data center, it is noted that thewater block 10 could operate at high inlet temperatures of up to 50° C., whereby water chillers for the water circulation system of the data center can be replaced by more preferable direct cooling solutions (e.g., dry coolers), which reduces costs and energy consumption associated with the implementation of water chillers. - With reference to
FIG. 4 , an alternative embodiment of thewater block 10 will be described. In this embodiment, thefluid conduit 30 of the above-described embodiment is replaced with afluid conduit 130. As will be noted, the path described by thefluid conduit 130 as defined by thebase 14 is different from thefluid conduit 30 described above. - The
fluid conduit 130 is thermally coupled to thethermal transfer surface 20 such that, when water flows in thefluid conduit 130, heat absorbed by thethermal transfer surface 20 is subsequently absorbed by water flowing in thefluid conduit 130. Water is received into thefluid conduit 130 via aninlet 132 and expelled therefrom via anoutlet 134. Both theinlet 132 and theoutlet 134 are defined in the cover 13 (i.e., water enters and exits thebody 12 via the cover 13). - The path described by the
fluid conduit 130 begins at theinlet 132 thereof which is located generally at a corner of therectangular water block 10. That is, theinlet 132 is located adjacent an intersection of thelongitudinal end 25 and thelateral end 31 of thebase 14. Thefluid conduit 130 branches into two channels 136 1, 136 2 at theinlet 32 such that the flow of fluid within thefluid conduit 130 is split between both channels 136 1, 136 2. As discussed above, this may promote laminar flow of fluid within thefluid conduit 130 which reduces pressure drop of the fluid as it flows through thefluid conduit 130. The channels 136 1, 136 2 extend parallel to one another along at least a majority of a span of thefluid conduit 130. More specifically, in this embodiment, the channels 136 1, 136 2 extend parallel and adjacent to one another from theinlet 132 to theoutlet 134. As will be described further below, the channels 136 1, 136 2 merge together again at theoutlet 134. However, in the span of thefluid conduit 130 between theinlet 132 and theoutlet 134, the channels 136 1, 136 2 are fluidly separate from one another such that water flow from both channels 136 1, 136 2 does not mix until reaching theoutlet 134. - It is contemplated that, in alternative embodiments, the
fluid conduit 130 could branch into more than two channels. For instance, the fluid conduit could branch into three channels or four channels. - Furthermore, it is contemplated that, in alternative embodiments, the junction at which the
fluid conduit 130 branches into the two channels 136 1, 136 2 could be at a location other than theinlet 132. For example, thefluid conduit 130 could branch into the two channels 136 1, 136 2 at a junction downstream from the inlet 132 (i.e., a location, along the path of thefluid conduit 130, further from the inlet 132). Similarly, it is contemplated that, in alternative embodiments, the junction at which the two channels 136 1, 136 2 merge together could be upstream from theoutlet 134. - The
fluid conduit 130 forms a “serpentine” path. As mentioned above, a serpentine path is herein defined as being a path that describes at least one S-shaped curve. More specifically, thefluid conduit 130 defines a plurality of longitudinally-extending sections 140 1-140 7 that are parallel to one another and are laterally spaced from one another, with adjacent ones of the longitudinally-extending sections 140 1-140 7 being connected by looping sections 144 1-144 6. By extension, the channels 136 1, 136 2 of thefluid conduit 130 extend generally parallel to one another along the serpentine path (i.e., along the longitudinally-extending sections 140 1-140 7 and the looping sections 144 1-144 6). - The
inlet 132 is located at the longitudinally-extending section 140 1 and theoutlet 134 is located at the longitudinally-extending section 140 7 such that theinlet 132 and theoutlet 134 are located at the laterally furthest-most of the longitudinally-extending sections 140 1-140 7 respectively (i.e., the longitudinally-extending sections 140 1-140 7 which are most laterally spaced from one another). Moreover, theinlet 132 and theoutlet 134 are generally located at diagonally opposite corners of the rectangular water block 10 (like illustrated inFIG. 4 , with an even number of looping sections 144 1-144 6). Therefore, although not illustrated herein, in this embodiment, the 16, 18 will be connected to thetubes cover 13 at the corresponding diagonally opposite corners (unlike what is illustrated inFIG. 1 ) to be connected to theinlet 132 and theoutlet 134. In alternative embodiments, as shown inFIG. 7 , theinlet 132 and theoutlet 134 may be located at laterally opposite corners adjacent the samelongitudinal end 25. In such embodiments, the number of looping sections 144 x would be uneven (see looping sections 144 1-144 5 inFIG. 7 ). - Furthermore, it is contemplated that, in alternative embodiments, the two channels 136 1, 136 2 could merge together at an intermediate junction between the
inlet 132 and theoutlet 134, such that thefluid conduit 130 defines a single channel downstream of the intermediate junction before thefluid conduit 130 splits again into two channels 146 1, 146 2. For example, as shown inFIG. 8 , the longitudinally-extending sections 140 1-140 3 are positioned, laterally, between theinlet 132 and an intermediate junction JCT1. The two channels 136 1, 136 2 extend along each of the longitudinally-extending sections 140 1-140 3 and looping sections 144 1, 144 2 interconnecting the longitudinally-extending sections 140 1-140 3. At the intermediate junction JCT1, the two channels 136 1, 136 2 merge into asingle channel 155 which, alone, defines the path of thefluid conduit 130 from the intermediate junction JCT1 to another intermediate junction JCT2 downstream from the intermediate junction JCT1. Thefluid conduit 130 defines a plurality of longitudinally-extending sections 145 1-145 3 that are parallel to one another and laterally spaced from one another, and extending between the intermediate junctions JCT1, JCT2. Thesingle channel 155 extends along the longitudinally-extending sections 145 1-145 3 and the looping sections interconnecting the longitudinally-extending sections 145 1-145 3. The longitudinally-extending sections 145 1-145 3 are substantially laterally centered between the lateral ends 29, 31 and define a limited region of thefluid conduit 130 where heat transfer is prioritized over pressure drop. This may be beneficial for example in cases where heat generation of theCPU 105 is greatest at its center. Thefluid conduit 130 again branches into two channels 146 1, 146 2 at the intermediate junction JCT2 downstream from the intermediate junction JCT1. Between the intermediate junction JCT2 and theoutlet 134, thefluid conduit 130 defines longitudinally-extending sections 140 4-140 6 positioned parallel to one another and laterally spaced from one another, similarly to the previous longitudinally-extending sections 140 1-140 3. The two channels 146 1, 146 2 extend along each of the longitudinally-extending sections 140 4-140 6 and looping sections 144 3, 144 4 interconnecting the longitudinally-extending sections 140 4-140 6. The two channels 146 1, 146 2 are configured similarly to the channels 136 1, 136 2—notably, the two channels 146 1, 146 2 extend parallel to one another along at least a majority (i.e., a majority or an entirety) of a span thereof and each of the channels 146 1, 146 2 also defines a sinusoidal pattern along at least a majority of a span thereof. The channels 146 1, 146 2 merge at theoutlet 134 downstream from the intermediate junction JCT2. As discussed above with regard toFIG. 4 , theoutlet 134 is located at a diagonally opposite corner from theinlet 132. In alternative embodiments, theinlet 132 and theoutlet 134 may be located at laterally opposite corners adjacent the samelongitudinal end 25, as discussed above with regard toFIG. 7 . - Each of the channels 136 1, 136 2 defines a sinusoidal pattern along a majority of a span thereof. That is, each one of the channels 136 1, 136 2 has a repetitive pattern approximating that of a sinusoidal function along at least half of the span of that channel 136 1, 136 2. In this case, the sinusoidal pattern is defined along the longitudinally-extending portions 140 1-140 7 of the serpentine path of the
fluid conduit 130. The sinusoidal pattern defined by the channels 136 1, 136 2 changes a direction of the flow of water within the channels 136 1, 136 2 as the flow of water engages the curves defined by the sinusoidal pattern. Moreover, it is noted that the channels 136 1, 136 2 have a constant width (i.e., a distance between the opposite walls of each of the channels 136 1, 136 2 is uniform along a span thereof) as the width is unaffected by the curves defined by the sinusoidal pattern. In particular, in this embodiment, the width of each of the channels 136 1, 136 2 is 2 mm. In other embodiments, the width of the channels of each of the channels 136 1, 136 2 may be between 1 mm and 4 mm. The channels 136 1, 136 2 may have any other suitable dimensions in other embodiments so long as it is convenient for the flow regime within the channels 136 1, 136 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router). - As in the previous embodiment, the
fluid conduit 130 is defined by thecover 13 and the base 14 when thecover 13 and the base 14 are affixed to one another. Moreover, in this embodiment, the path of the fluid conduit 130 (including the path of each of the channels 136 1, 136 2) is defined by the base 14 independently of thecover 13. In other words, while thecover 13 defines part of the fluid conduit 130 (covering an open top thereof), the direction of the water flow within thefluid conduit 30 is defined by therecess 115 machined into theupper surface 24 of thebase 14. For its part, thecover 13 has a lower flat surface that closes the open top of the recess 115 (except at theinlet 132 and the outlet 134). With reference toFIG. 5 , another alternative embodiment of thewater block 10 will be described. In this embodiment, thefluid conduit 30 is replaced with afluid conduit 230. As will be noted, the path described by thefluid conduit 230 as defined by thebase 14 is different from the 30, 130 described above.fluid conduits - The
fluid conduit 230 is thermally coupled to thethermal transfer surface 20 such that, when water flows in thefluid conduit 230, heat absorbed by thethermal transfer surface 20 is subsequently absorbed by water flowing in thefluid conduit 230. Water is received into thefluid conduit 230 via aninlet 232 and expelled therefrom via anoutlet 234. Both theinlet 232 and theoutlet 234 are defined in the cover 13 (i.e., water enters and exits thebody 12 via the cover 13). - The path described by the
fluid conduit 230 begins at theinlet 232 thereof which is located generally centrally of the rectangular water block 10 (i.e., laterally and longitudinally centered between the lateral and longitudinal ends thereof). The central position of theinlet 232 allows routing cool water to the center of thewater block 10, which may be beneficial if the location of theCPU 105 that is most desired to be cooled is centrally located. Notably, water will be coolest along thefluid conduit 230 at the central inlet 232 (since the water has not yet absorbed heat from circulating through an appreciable span of the fluid conduit 230) and therefore heat transfer at the center of the CPU 105 (i.e., a position aligned with the inlet 232) will be significant. - The
fluid conduit 230 branches into two channels 236 1, 236 2 at theinlet 232 such that the flow of fluid within thefluid conduit 230 is split between both channels 236 1, 236 2. As discussed above, this may promote laminar flow of fluid within thefluid conduit 230 which reduces pressure drop of the fluid as it flows therethrough. The channels 236 1, 236 2 extend parallel to one another along at least a majority of a span of thefluid conduit 230. More specifically, in this embodiment, the channels 236 1, 236 2 extend parallel from theinlet 232 to theoutlet 234. As will be described further below, the channels 236 1, 236 2 merge together again at theoutlet 234. However, in the span of thefluid conduit 230 between theinlet 232 and theoutlet 234, the channels 236 1, 236 2 are fluidly separate from one another such that water flow from both channels 236 1, 236 2 does not mix until reaching theoutlet 234. - It is contemplated that, in alternative embodiments, the
fluid conduit 230 could branch into more than two channels. For instance, the fluid conduit could branch into three channels or four channels. - Furthermore, it is contemplated that, in alternative embodiments, the junction at which the
fluid conduit 230 branches into the two channels 236 1, 236 2 could be at a location other than theinlet 232. For example, as shown inFIG. 9 , thefluid conduit 230 could branch into the two channels 236 1, 236 2 at a junction JCT downstream from the inlet 232 (i.e., a location, along the path of thefluid conduit 230, further from the inlet 232). This configuration may be advantageous to prioritize heat transfer at a given region of thefluid conduit 230. For instance, in such a configuration as that depicted inFIG. 9 , heat transfer in the region from theinlet 232 to the junction JCT may be greater than in the remainder of thefluid conduit 230 while incurring some pressure drop in the water in this limited region of the fluid conduit 230 (since the water flow is not split into the two channels 236 1, 236 2 in this region). Similarly, it is contemplated that, in alternative embodiments, the junction at which the two channels 236 1, 236 2 merge together could be upstream from theoutlet 234. - Each of the channels 236 1, 236 2 has a constant width (i.e., a distance between the opposite walls of each of the channels 236 1, 236 2 is uniform along a span thereof). In particular, in this embodiment, the width of each of the channels 236 1, 236 2 is 2 mm. In other embodiments, the width of the channels of each of the channels 236 1, 236 2 may be between 1 mm and 4 mm. The channels 236 1, 236 2 may have any other suitable dimensions in other embodiments, so long as it is convenient for the flow regime within the channels 236 1, 236 2 and easily machinable such as with a machine tool having a rotary cutter (e.g., a mill or a router).
- The
fluid conduit 230 forms a generally rectangular spiral path centered about theinlet 232. More specifically, the path of thefluid conduit 230 begins at theinlet 232 and extends further away from theinlet 232 as it revolves around theinlet 232. The spiral path of thefluid conduit 230 ends at theoutlet 234 which is positioned at an outer periphery of the spiral path formed by thefluid conduit 230. In particular, the spiral path of thefluid conduit 230 is formed by ring sections 250 1-250 5 of thefluid conduit 230. The ring sections 250 1-250 5 are concentric about theinlet 232. Theinnermost ring section 250 1 is closest to theinlet 232 and theoutermost ring section 250 5 is furthest form theinlet 232. In particular, theoutlet 234 is located at theoutermost ring section 250 5. Since theoutlet 234 is located generally at a corner of therectangular water block 10, the spiral path of thefluid conduit 230 spreads across almost an entirety of the area of the water block 10 (i.e., therecess 215 in theupper surface 24 of thebase 14 spans most of a length and a width of the base 14). - In this embodiment, the rectangular spiral path of the
fluid conduit 230 is generally square (i.e., the length and width of thefluid conduit 230 are approximately similar). However, in some cases, the length of the spiral path of thefluid conduit 230 be greater than its width. This may better accommodate the rectangular shape of the CPU 105 (or other component to be cooled). - The spiral path of the
fluid conduit 230 does not include many tight curves (i.e., the radius of curvature of most if not all curves is relatively large) which facilitates and speeds up machining of therecess 215 in thebase 14. Moreover, the radius of curvature of the curves of the spiral path may increase in proportion to a distance of the curve relative to theinlet 232. That is, the further from the central inlet 232 a curve of the spiral path is, the greater its radius of curvature. - As in the previous embodiments, the
fluid conduit 230 is defined by thecover 13 and the base 14 when thecover 13 and the base 14 are affixed to one another. Moreover, in this embodiment, the path of the fluid conduit 230 (including the path of each of the channels 236 1, 236 2) is defined by the base 14 independently of thecover 13. In other words, while thecover 13 defines part of the fluid conduit 230 (covering an open top thereof), the direction of the water flow within thefluid conduit 230 is defined by therecess 215 machined into theupper surface 24 of thebase 14. For its part, thecover 13 has a lower flat surface that closes the open top of the recess 215 (except at theinlet 132 and the outlet 134). - In some embodiments, the cover and base may be affixed to one another differently. For instance, as shown in
FIG. 6 , acover 13′ and a base 14′ are affixed to one another by fasteners 19 (e.g., screws). In such an embodiment, thecover 13′ has holes extending therethrough for receiving thefasteners 19, and the base 14′ has corresponding receiving openings (not shown) that are threaded to receive thefasteners 19. A sealing member (e.g., a gasket) may be received between thecover 13′ and the base 14′ to prevent leaks from within the fluid conduit (which can have any of the configurations discussed above with respect to the 30, 130, 230). Moreover, in this embodiment, thefluid conduits cover 13′ is made of a polymeric material (the base 14′ is still made of copper). For instance, thecover 13′ may be an injection molded component. In this embodiment, the 16, 18 are also made of polymeric material. A resin may seal the interface between thetubes 16, 18 and thetubes cover 13′. - While the
thermal transfer device 10 has been described above as being configured for absorbing heat from thetarget component 105, it is contemplated that, in alternative embodiments, thethermal transfer device 10 could be used for transferring heat to the target component 105 (in such a case, the target component is not a CPU). - The
thermal transfer device 10 implemented in accordance with some non-limiting embodiments of the present technology can be represented as presented in the following numbered clauses. - CLAUSE 1. A thermal transfer device (10), comprising: a body (12) having a thermal transfer surface (20) configured to be placed in contact with a target component (105); a fluid conduit (230) defined in the body (12) and configured for conveying fluid through the body (12), the fluid conduit (230) being thermally coupled to the thermal transfer surface (20), the fluid conduit (230) having an inlet (232) and an outlet (234) wherein: the fluid conduit (230) forms a generally spiral path; the inlet (232) is positioned at a center of the spiral path; at a first junction, the fluid conduit (230) branches into at least two channels (236 1, 236 2) extending generally parallel to one another throughout at least a majority of the span of the fluid conduit (230); and the at least two channels (236 1, 236 2) merge at a second junction.
- CLAUSE 2. The thermal transfer device of clause 1, wherein the first junction is the inlet (232) of the fluid conduit (230).
-
CLAUSE 3. The thermal transfer device of clause 1 or 2, wherein the second junction is the outlet (234) of the fluid conduit (230). - CLAUSE 4. The thermal transfer device of any one of clauses 1 to 3, wherein the spiral path is a generally square spiral path.
- CLAUSE 5. The thermal transfer device of any one of clauses 1 to 4, wherein the outlet (234) is positioned at an outer periphery of the spiral path formed by fluid conduit (230).
- CLAUSE 6. The thermal transfer device of any one of clauses 1 to 5, wherein a width of each of the at least two channels (236 1, 236 2) is constant.
- CLAUSE 7. The thermal transfer device of clause 6, wherein the width of each of the at least two channels (236 1, 236 2) is between 1 mm and 4 mm inclusively.
- CLAUSE 8. The thermal transfer device of any one of clauses 1 to 7, wherein: the body (12) comprises a first body portion (14) and a second body portion (13) affixed to the first body portion (14); the fluid conduit (230) is defined by the first and second body portions (14, 13); and a path of each of the at least two channels (236 1, 236 2) is defined by the first body portion (14).
- CLAUSE 9. The thermal transfer device of clause 8, wherein the inlet (232) and the outlet (234) are defined in the second body portion (13).
-
CLAUSE 10. The thermal transfer device of clause 8, wherein the first and second body portions (14, 13) are welded to one another. - CLAUSE 11. The thermal transfer device of any one of clauses 1 to 10 being a water block.
-
CLAUSE 12. The thermal transfer device of clause 11, wherein the water block is generally rectangular. -
CLAUSE 13. A thermal transfer device (10), comprising: a body (12) having a thermal transfer surface (20) configured to be placed in contact with a target component (105); a fluid conduit (130) defined in the body (12) and configured for conveying fluid through the body (12), the fluid conduit (130) being thermally coupled to the thermal transfer surface (20), the fluid conduit (130) having an inlet (132) and an outlet (134), wherein: the fluid conduit (130) forms a serpentine path; at a first junction, the fluid conduit (130) branches into at least two channels (136 1, 136 2) extending generally parallel to one another along the serpentine path formed by the fluid conduit (130); each of the at least two channels (136 1, 136 2) defines a sinusoidal pattern along at least a majority of a span thereof; and the at least two channels (136 1, 136 2) merge at a second junction. -
CLAUSE 14. The thermal transfer device ofclause 13, wherein the first junction is the inlet (132) of the fluid conduit (130). -
CLAUSE 15. The thermal transfer device of 13 or 14, wherein the second junction is the outlet (134) of the fluid conduit (130).clause -
CLAUSE 16. The thermal transfer device of any one ofclauses 13 to 15, wherein: the serpentine path formed by the fluid conduit (130) defines a plurality of longitudinally-extending sections (140 1-140 7) that are parallel to one another and laterally spaced from one another; the plurality of longitudinally-extending sections (140 1-140 7) includes a first longitudinally-extending section (140 1) and a second longitudinally-extending section (140 7) that are laterally furthest-most of the longitudinally-extending sections (140 1-140 7); the first junction is located at the first longitudinally-extending section (140 1); and the second junction is located at the second longitudinally-extending section (140 7). - CLAUSE 17. The thermal transfer device of any one of
clauses 13 to 16, wherein a width of each of the at least two channels (136 1, 136 2) is constant. -
CLAUSE 18. The thermal transfer device of clause 17, wherein the width of each of the at least two channels (136 1, 136 2) is between 1 mm and 4 mm inclusively. -
CLAUSE 19. The thermal transfer device ofclause 13, wherein: the second junction is a first intermediate junction (JCT1) downstream from the first junction; the fluid conduit (130) branches into an other at least two channels (146 1, 146 2) at a second intermediate junction (JCT2) between the first intermediate junction (JCT1) and the outlet (134); between the first and second intermediate junctions (JCT1, JCT2), the fluid conduit (130) defines a plurality of longitudinally-extending sections (145 1-145 3) that are parallel to one another and laterally spaced from one another, the fluid conduit (130) having a single channel (155) extending along the longitudinally-extending sections (145 1-145 3); the longitudinally-extending sections (145 1-145 3) are substantially laterally centered between lateral ends of the body (12); the other at least two channels (146 1, 146 2) merge at a fourth junction. -
CLAUSE 20. The thermal transfer device ofclause 19, wherein each of the other at least two channels (146 1, 146 2) defines a sinusoidal pattern along at least a majority of a span thereof. - CLAUSE 21. The thermal transfer device of any one of
clauses 13 to 20, wherein the serpentine path of the fluid conduit (130) extends from the inlet (132) to the outlet (134). -
CLAUSE 22. The thermal transfer device of any one ofclauses 13 to 19, wherein: the body (12) comprises a first body portion (14) and a second body portion (13) affixed to the first body portion (14); the fluid conduit (130) is defined by the first and second body portions (14, 13); and a path of each of the at least two channels (136 1, 136 2) is defined by the first body portion (14). - CLAUSE 23. The thermal transfer device of
clause 22, wherein the inlet (132) and the outlet (134) are defined in the second body portion (13). -
CLAUSE 24. The thermal transfer device ofclause 22, wherein the first and second body portions (14, 13) are welded to one another. -
CLAUSE 25. The thermal transfer device of any one ofclauses 13 to 22 being a water block. - CLAUSE 26. The thermal transfer device of
clause 25, wherein the water block is generally rectangular. -
CLAUSE 27. The thermal transfer device of clause 26, wherein the inlet (132) and the outlet (134) are generally located at diagonally opposite corners of the rectangular water block. - CLAUSE 28. The thermal transfer device of clause 26, wherein the inlet (132) and the outlet (134) are generally located at laterally opposite corners of the rectangular water block.
- Modifications and improvements to the above-described embodiments of the present technology may become apparent to those skilled in the art. The foregoing description is intended to be exemplary rather than limiting. The scope of the present technology is therefore intended to be limited solely by the scope of the appended claims.
Claims (20)
1. A water block for cooling one of a central processing unit (CPU) and a graphics processing unit (GPU) of a computer system, the water block comprising:
a body having a thermal transfer surface configured to be placed in contact with the one of the CPU and the GPU;
a fluid conduit defined in the body and configured for conveying fluid through the body, the fluid conduit being thermally coupled to the thermal transfer surface, the fluid conduit having an inlet and an outlet, the fluid conduit being configured so that:
at a first junction, the fluid conduit branches into a first channel and a second channel which extend adjacent and generally parallel to one another along an initial portion of the fluid conduit;
the first and second channels diverge away from one another at an end of the initial portion such that each of the first and second channels forms a serpentine path, the serpentine path formed by the first channel extending toward a first direction, the serpentine path formed by the second channel extending toward a second direction generally opposite to the first direction;
the first and second channels merge at a second junction; and
each of the first and second channels defines a sinusoidal pattern along at least a majority of a span thereof.
2. The water block of claim 1 , wherein the first junction is the inlet of the fluid conduit.
3. The water block of claim 1 , wherein the second junction is the outlet of the fluid conduit.
4. The water block of claim 1 , wherein a width of each of the first and second channels is constant.
5. The water block of claim 4 , wherein the width of each of the first and second channels is between 1 mm and 4 mm inclusively.
6. The water block of claim 1 , wherein:
the serpentine path formed by each of the first and second channels defines a plurality of longitudinally-extending sections that are parallel to one another and laterally spaced from one another; and
the plurality of longitudinally-extending sections includes an innermost longitudinally-extending section that is closest to the first junction and an outermost longitudinally-extending section that is furthest from the first junction.
7. The water block of claim 6 , wherein the inlet is located centrally between the outermost longitudinally-extending section of the first channel and the outermost longitudinally-extending section of the second channel.
8. The water block of claim 7 , wherein the outlet is laterally aligned with the inlet.
9. The water block of claim 1 , wherein the first and second channels extend in opposite directions from the second junction.
10. The water block of claim 1 , wherein:
the body comprises a first body portion and a second body portion affixed to the first body portion;
the fluid conduit is defined by the first and second body portions; and
a path of each of the first and second channels is defined by the first body portion.
11. The water block of claim 10 , wherein the inlet and the outlet are defined in the second body portion.
12. The water block of claim 10 , wherein the first and second body portions are welded to one another.
13. The water block of claim 1 , wherein the water block is generally rectangular.
14. The water block of claim 6 , wherein:
each of the plurality of longitudinally-extending sections defines the sinusoidal pattern of the first and second channels; and
the sinusoidal pattern defined by each of the plurality of longitudinally-extending sections is nested with the sinusoidal pattern defined by an adjacent one of the plurality of longitudinally-extending sections.
15. A thermal transfer device, comprising:
a body having a thermal transfer surface configured to be placed in contact with a target component;
a fluid conduit defined in the body and configured for conveying fluid through the body, the fluid conduit being thermally coupled to the thermal transfer surface, the fluid conduit having an inlet and an outlet, the fluid conduit being configured so that:
at a first junction, the fluid conduit branches into a first channel and a second channel which extend adjacent and generally parallel to one another along an initial portion of the fluid conduit;
the first and second channels diverge away from one another at an end of the initial portion such that each of the first and second channels forms a serpentine path, the serpentine path formed by the first channel extending toward a first direction, the serpentine path formed by the second channel extending toward a second direction generally opposite to the first direction; and
the first and second channels merge at a second junction.
16. The thermal transfer device of claim 15 , wherein the first junction is the inlet of the fluid conduit.
17. The thermal transfer device of claim 15 , wherein the second junction is the outlet of the fluid conduit.
18. The thermal transfer device of claim 15 , wherein each of the first and second channels defines a sinusoidal pattern along at least a majority of a span thereof.
19. The thermal transfer device of claim 15 , wherein a width of each of the first and second channels is constant.
20. The thermal transfer device of claim 19 , wherein the width of each of first and second channels is between 1 mm and 4 mm inclusively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US17/176,454 US11644254B2 (en) | 2018-09-04 | 2021-02-16 | Thermal transfer device having a fluid conduit |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP18315027.5A EP3620741B1 (en) | 2018-09-04 | 2018-09-04 | Thermal transfer device having a fluid conduit |
| EP18315027.5 | 2018-09-04 |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US17/176,454 Continuation US11644254B2 (en) | 2018-09-04 | 2021-02-16 | Thermal transfer device having a fluid conduit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20200072565A1 true US20200072565A1 (en) | 2020-03-05 |
Family
ID=63713800
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US16/546,785 Abandoned US20200072565A1 (en) | 2018-09-04 | 2019-08-21 | Thermal transfer device having a fluid conduit |
| US17/176,454 Active 2039-09-20 US11644254B2 (en) | 2018-09-04 | 2021-02-16 | Thermal transfer device having a fluid conduit |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US17/176,454 Active 2039-09-20 US11644254B2 (en) | 2018-09-04 | 2021-02-16 | Thermal transfer device having a fluid conduit |
Country Status (6)
| Country | Link |
|---|---|
| US (2) | US20200072565A1 (en) |
| EP (2) | EP3620741B1 (en) |
| CN (1) | CN110874127B (en) |
| CA (1) | CA3052817A1 (en) |
| DK (2) | DK3620741T3 (en) |
| PL (2) | PL3620741T3 (en) |
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| CN113675178A (en) * | 2020-07-30 | 2021-11-19 | 台湾积体电路制造股份有限公司 | Semiconductor package, semiconductor device and forming method thereof |
| US20220276008A1 (en) * | 2021-02-26 | 2022-09-01 | Teradyne, Inc. | Thermal plate having a fluid channel |
| WO2023287449A1 (en) * | 2021-07-12 | 2023-01-19 | Sensata Technologies, Inc. | System and method for cooling high power electrical systems |
| US20240074107A1 (en) * | 2022-08-29 | 2024-02-29 | Ovh | Cooling block for cooling a heat-generating electronic component and method for manufacturing thereof |
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| US12402287B2 (en) * | 2020-05-29 | 2025-08-26 | Ovh | Uninterruptible power supply having a liquid cooling device |
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-
2019
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2021
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3735565A4 (en) * | 2018-01-05 | 2021-09-29 | Baltimore Aircoil Company, Inc. | INDIRECT HEAT EXCHANGER |
| US12402287B2 (en) * | 2020-05-29 | 2025-08-26 | Ovh | Uninterruptible power supply having a liquid cooling device |
| CN113675178A (en) * | 2020-07-30 | 2021-11-19 | 台湾积体电路制造股份有限公司 | Semiconductor package, semiconductor device and forming method thereof |
| US11996351B2 (en) | 2020-07-30 | 2024-05-28 | Taiwan Semiconductor Manufacturing Co., Ltd. | Packaged semiconductor device including liquid-cooled lid and methods of forming the same |
| US20220276008A1 (en) * | 2021-02-26 | 2022-09-01 | Teradyne, Inc. | Thermal plate having a fluid channel |
| US12287151B2 (en) * | 2021-02-26 | 2025-04-29 | Teradyne, Inc. | Thermal plate having a fluid channel |
| WO2023287449A1 (en) * | 2021-07-12 | 2023-01-19 | Sensata Technologies, Inc. | System and method for cooling high power electrical systems |
| US11917799B2 (en) | 2021-07-12 | 2024-02-27 | Sensata Technologies, Inc. | System and method for cooling high power electrical systems |
| US20240074107A1 (en) * | 2022-08-29 | 2024-02-29 | Ovh | Cooling block for cooling a heat-generating electronic component and method for manufacturing thereof |
| EP4589235A1 (en) * | 2024-01-18 | 2025-07-23 | Rimac Technology LLC | Heat exchange assembly |
Also Published As
| Publication number | Publication date |
|---|---|
| PL3792576T3 (en) | 2023-02-20 |
| PL3620741T3 (en) | 2021-05-31 |
| US20210164738A1 (en) | 2021-06-03 |
| US11644254B2 (en) | 2023-05-09 |
| DK3792576T3 (en) | 2023-01-09 |
| CN110874127A (en) | 2020-03-10 |
| DK3620741T3 (en) | 2021-03-01 |
| CN110874127B (en) | 2022-07-12 |
| CA3052817A1 (en) | 2020-03-04 |
| EP3620741B1 (en) | 2021-01-27 |
| EP3792576B1 (en) | 2022-12-21 |
| EP3792576A1 (en) | 2021-03-17 |
| EP3620741A1 (en) | 2020-03-11 |
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