Nucleate boiling apparatus and computing system
By designing staggered pipe layers in the nucleus boiling device, the problem of uneven bubble distribution was solved, achieving more efficient heat conduction and heat dissipation, resolving the problem of localized hot spots, and improving the security of the computing system.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- QUANTA COMPUTER INC
- Filing Date
- 2022-04-07
- Publication Date
- 2026-07-14
Smart Images

Figure CN115729328B_ABST
Abstract
Description
Technical Field
[0001] The present invention relates to an apparatus for promoting nucleus boiling to cool a component that generates heat within a computing system, and more specifically, to a nucleus boiling apparatus that provides two separate nucleus boiling point layers. Background Technology
[0002] Two-phase boiling heat transfer is a thermal solution for densely powered components within computing systems. The latent heat of the phase change readily dissipates a significant amount of heat while maintaining the component temperature at its saturation point. Figure 1 This illustrates a situation where a core-shaped boiling plate 100 is in contact with a component (not shown) generating heat within a computing system (not shown). Due to this excellent heat dissipation performance, boiling heat transfer plays a crucial role in future thermal solutions. However, excessive heat dissipation and uneven distribution create localized hot spots, causing bubbles to coalesce into a bubble film in a downstream region. This reduces boiling heat transfer and, in the worst case, can cause component burnout. Figure 1 The bubble membrane 101 is shown relative to the core boiling plate 100.
[0003] To prevent this problem, please refer to Figure 2 A reinforced nucleus boiling plate 200 is commonly used to generate bubbles more uniformly on the surface. This reinforced nucleus boiling plate 200 is typically made of a highly thermally conductive material (e.g., copper) and includes a surface treatment, such as coating with microparticles or stamped dimples 202, to enhance nucleus boiling. Figure 2 Display, with Figure 1 Compared to the original nucleus-shaped boiling plate 100, the enhanced nucleus-shaped boiling plate 200 successfully enables steam bubbles to form more uniformly over almost all of its surface areas. However, it does not completely prevent large-deformation steam bubbles 201 in the center from affecting the heat dissipation of the entire enhanced nucleus-shaped boiling plate 200.
[0004] The present invention aims to provide a nucleo boiling device that solves the above-mentioned problems and other needs. Summary of the Invention
[0005] The terms used in the description of embodiments, and similar terms (e.g., implementation, configuration, feature, example, and option), are intended to refer broadly to all aspects of the invention and the appended claims. Several statements containing these terms should be understood as not limiting the subject matter described herein or limiting the meaning or scope of the appended claims. The embodiments of the invention covered herein are defined by the appended claims, not by the scope of the invention itself. This summary is a high-level overview of various features of the invention and introduces some concepts further described in the following description paragraphs. This summary is not intended to identify key or essential features of the subject matter of the claims, nor is it intended to be used independently to determine the scope of the subject matter of the claims. The subject matter should be understood through reference to appropriate portions of the complete specification of the invention, any or all of the accompanying drawings, and each claim.
[0006] According to a feature of the present invention, a nucleoboiling device is disclosed, comprising a base configured to be mounted on a heated object to provide immersion cooling of the object in a liquid cooling computational environment. The base is defined by an upper surface, a lower surface, and a plurality of side surfaces. The plurality of side surfaces include a first side surface and a second side surface. The nucleoboiling device further includes a first set of a plurality of conduits extending from the first side surface. The first set of a plurality of conduits includes a first transition region and a first flat region. In the first transition region, the first set of a plurality of conduits extends away from the base along a first inclined direction relative to the base. In the first flat region, the first set of a plurality of conduits extends away from the base in a fan-shaped outward arrangement. The nucleoboiling device further includes a second set of a plurality of conduits extending from a second side surface. The second set of a plurality of conduits includes a second transition region and a second flat region. In the second transition region, the second set of a plurality of conduits extends away from the base along a second inclined direction relative to the base. In the second flat region, the second set of a plurality of conduits extends away from the base in a fan-shaped outward arrangement. The distance between the second flat area and the upper surface of the base is greater than the distance between the first flat area and the upper surface of the base.
[0007] According to one embodiment of the above features, in a first flat region, the surface of the first group of multiple pipes includes one or more features that enhance nucleus boiling. According to another embodiment of the above features, in a second flat region, the surface of the second group of multiple pipes includes one or more features that enhance nucleus boiling. According to another embodiment of the above features, the first group of multiple pipes is connected to the second group of multiple pipes via a base, such that each pipe of the first group of multiple pipes is connected to a corresponding pipe of the second group of multiple pipes to form a single pipe. According to another embodiment of the above features, the first group of multiple pipes is arranged in a single layer. According to another embodiment of the above features, the second group of multiple pipes is arranged in a single layer. According to another embodiment of the above features, the first group of multiple pipes includes eight pipes. According to another embodiment of the above features, the second group of multiple pipes includes eight pipes. According to another embodiment of the above features, in a first transition region, the first group of multiple pipes is inclined at a first angle relative to the base, and in a second transition region, the second group of multiple pipes is inclined at a second angle relative to the base, and the second angle is different from the first angle. According to another embodiment of the above features, in the first flat region, the cross-sectional area of each pipe of the first group of multiple pipes is larger than the cross-sectional area in the first transition region. According to another embodiment of the above features, in the first flat region, the cross-sectional area of each pipe in the first group of multiple pipes increases with distance from the base. According to another embodiment of the above features, in the second flat region, the cross-sectional area of each pipe in the second group of multiple pipes is larger than the cross-sectional area in the second transition region. According to another embodiment of the above features, in the second flat region, the cross-sectional area of each pipe in the second group of multiple pipes increases with distance from the base. According to another embodiment of the above features, in the first transition region, all pipes in the first group of multiple pipes are parallel to each other. According to another embodiment of the above features, in the second transition region, all pipes in the second group of multiple pipes are parallel to each other. According to another embodiment of the above features, in the first flat region, the spacing between the outer pipes of the first group of multiple pipes is greater than the spacing between the inner pipes of the first group of multiple pipes. According to another embodiment of the above features, in the second flat region, the spacing between the outer pipes of the second group of multiple pipes is greater than the spacing between the inner pipes of the second group of multiple pipes. According to another embodiment of the above features, each pipe in both the first group of multiple pipes and the second group of multiple pipes is a sealed hollow metal pipe containing a working fluid. According to another embodiment of the above features, the first group of multiple pipes and the second group of multiple pipes span a width less than that of the base.
[0008] According to another feature of the invention, a computing system is disclosed, including a processor and a nucleus boiling device. The nucleus boiling device has a base defined by an upper surface, a lower surface, and a plurality of side surfaces. The plurality of side surfaces include a first side surface and a second side surface. The lower surface contacts or is close to the processor. The nucleus boiling device also includes a first set of a plurality of conduits extending from the first side surface. The first set of a plurality of conduits includes a first transition region and a first flat region. In the first transition region, the first set of a plurality of conduits extends away from the base along a first inclined direction relative to the base. In the first flat region, the first set of a plurality of conduits extends outward in a first fan shape perpendicular to the first side surface. The nucleus boiling device also includes a second set of a plurality of conduits extending from a second side surface. The second set of a plurality of conduits includes a second transition region and a second flat region. In the second transition region, the second set of a plurality of conduits extends away from the base along a second inclined direction relative to the base. In the second flat region, the second set of a plurality of conduits extends outward in a second fan shape perpendicular to the second side surface. The distance between the second flat area and the upper surface of the base is greater than the distance between the first flat area and the upper surface of the base.
[0009] The foregoing description is not intended to present every embodiment or feature of the invention. Rather, it provides only examples of some novel features and characteristics set forth herein. The above features and advantages, as well as other features and advantages, will become apparent from the following detailed description of representative embodiments and modes for carrying out the invention, taken in conjunction with the accompanying drawings and appended claims. Additional features of the invention will be apparent to those skilled in the art from the following brief description of various embodiments with reference to the accompanying drawings and the provided symbols. Attached Figure Description
[0010] The invention and its advantages, along with the accompanying drawings, will be better understood from the following description of exemplary embodiments in conjunction with the accompanying drawings. These drawings depict exemplary embodiments only and should therefore not be construed as limiting the various embodiments or claims.
[0011] Figure 1 This is a view of a nucleus-shaped boiling plate used for cooling within a computing system.
[0012] Figure 2 A view of an enhanced nucleus-boiling plate used for cooling within a computing system;
[0013] Figure 3A As a feature of the present invention, a side view of a core-shaped boiling device;
[0014] Figure 3BAs a feature of the present invention, a bottom view of a core-shaped boiling device;
[0015] Figure 3C As a feature of the present invention, a top view of a core-shaped boiling device;
[0016] Figure 4 As a feature of the present invention, a cavitation fraction distribution diagram in a computational fluid dynamics simulation of a nucleus boiling device;
[0017] Figure 5 As a feature of the present invention, a temperature distribution map of a computational fluid dynamics simulation of a nucleus boiling device is provided.
[0018] This invention is readily adaptable to various modifications and alternatives. Representative embodiments have been shown by way of example in the accompanying drawings and will be described in detail herein. However, it should be understood that this invention is not intended to be limited to the specific forms disclosed. Rather, this invention is intended to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined in the claims.
[0019] Symbol Explanation
[0020] 10: Components
[0021] 20: Fluid Flow (arrow)
[0022] 100: Core-shaped boiling plate
[0023] 101: Bubble Film
[0024] 200: Enhanced core-shaped boiling plate
[0025] 201: Central Large Deformation Steam Bubble
[0026] 202: Stamping recess
[0027] 300: Nucleus boiling equipment
[0028] 302: Group 1 multiple pipelines
[0029] 304: Second group of multiple pipes
[0030] 306: Base
[0031] 306a: Upper surface
[0032] 306b: Lower surface
[0033] 306c, 306e: Side surface
[0034] 306f: First side surface
[0035] 306d: Second side surface
[0036] 308: First flat area
[0037] 310: First Transition Zone
[0038] 312: Second flat area
[0039] 314: Second Transition Zone
[0040] 316a~316h: Piping
[0041] 318: Thermal interface materials
[0042] 320: Stamping recess
[0043] θ1: First angle
[0044] θ2: Second angle
[0045] D1, D2: Distance Detailed Implementation
[0046] Various embodiments are described with reference to the accompanying drawings, throughout which similar reference numerals are used to designate similar or equivalent elements. The drawings are not drawn to scale and are provided solely to illustrate the features and characteristics of the invention. It should be understood that many specific details, relationships, and methods are set forth to provide a comprehensive understanding. However, those skilled in the art will readily appreciate that various embodiments may be practiced without one or more specific details or in other ways. In some cases, well-known structures or operations are not shown in detail for illustrative purposes. The various embodiments are not limited to the order in which actions or events are shown, as some actions may occur in different orders and / or simultaneously with other actions or events. Furthermore, not all actions or events shown are necessary for implementing certain features and characteristics of the invention.
[0047] For the purposes of this embodiment, unless explicitly stated otherwise, the singular includes the plural and vice versa. The term "including" means "including but not limited to". Furthermore, approximate words such as "about (about), almost, substantially, approximatelyly" and similar words may be meant herein as, for example, "at," "near, nearly at," "within 3-5% of," "within acceptable manufacturing tolerances," or any logical combination thereof. Similarly, the terms "vertical" or "horizontal" are intended to additionally include "within 3-5%" in the vertical or horizontal direction, respectively. Furthermore, directional terms such as "top," "bottom," "left," "right," "above," and "below" are intended to relate to the equivalent directions depicted in the reference illustrations; to be understood from the context of the referenced object or element, such as from its usual location; or other such descriptions.
[0048] Figure 3A Showing a side view of a nucleus boiling device 300 according to a feature of the invention. The nucleus boiling device 300 includes a first set of multiple pipes 302, a second set of multiple pipes 304, and a base 306.
[0049] The base 306 is configured to mount a heat-generating component 10 (e.g., a processor) within a computing system to provide immersion cooling for the component 10 in a liquid-cooled computing environment. The base 306 utilizes an upper surface 306a ( Figure 3C ), the following surface 306b ( Figure 3BThe base 306 is defined by a plurality of side surfaces 306c to 306f. The plurality of side surfaces 306c to 306f include a first side surface 306f and a second side surface 306d opposite to the first side surface 306f. The base 306 may be made of a metal or a metal alloy, such as copper or an aluminum alloy. The primary purpose of the base 306 is to keep the first set of plurality of conduits 302 and the second set of plurality of conduits 304 substantially close to or abutting against the component 10. The diamond-hashed region of the base 306 represents the area where the first set of plurality of conduits 302 and the second set of plurality of conduits 304 extend through the base 306 to contact the component 10. In one or more embodiments, this contact may constitute direct contact between the base 306 and / or the plurality of conduits 302 and the plurality of conduits 304 and the component 10. Alternatively, this contact may involve the base 306 and / or the plurality of conduits 302 and the plurality of conduits 304 partially or completely contacting a thermal interface material 318 between the base 306 and the component 10. The thermal interface material 318 may improve heat transfer between the base 306 and / or the plurality of conduits 302 and the plurality of conduits 304 and the component 10.
[0050] A first set of multiple conduits 302 extends from a first side surface 306f of the base 306. The first set of multiple conduits 302 includes a first flat region 308 and a first transition region 310. In the first transition region 310, the first set of multiple conduits 302 is relative to... Figure 3A The orientation shown extends away from the base 306 along a first inclined direction relative to the base 306. In the first flat area 308, a first group of multiple pipes 302 extend outward from the base 306 in a fan-shaped arrangement, as follows: Figure 3B as well as Figure 3C As shown and further described. In the first transition region 310, all pipes within the first group of multiple pipes 302 are generally parallel to each other.
[0051] Similar to the first set of multiple conduits 302, the second set of multiple conduits 304 extends from the second side surface 306d of the base 306, opposite to the first set of multiple conduits 302 and the first side surface 306f. The second set of multiple conduits 304 includes a second flat region 312 and a second transition region 314. In the second transition region 314, the second set of multiple conduits 304 is related to... Figure 3A The orientation shown extends away from the base 306 along a second inclined direction relative to the base 306. In the second flat area 312, the second group of multiple pipes 304 extend outward from the base 306 in a fan-shaped arrangement, as follows: Figure 3B as well as Figure 3C As shown and further described. In the second transition zone 314, all pipes within the second group of multiple pipes 304 are generally parallel to each other.
[0052] To achieve improved immersion cooling, the distance between the second flat region 312 of the second set of multiple conduits 304 and the upper surface of the base 306 is greater than the distance between the first flat region 308 of the first set of multiple conduits 302 and the upper surface of the base 306. The second flat region 312 is located above the first flat region 308 on the base 306 to minimize the impact of bubble formation in one region on the other. Bubbles formed in one region can pass above or below the other region to reduce their impact on the opposite region. More specifically, the nucleus boiling device 300 can be positioned on component 10, which is located within a cooling liquid flow indicated by arrow 20 within a computing system. The first set of multiple conduits 302 can constitute the upstream region of the nucleus boiling device 300 within the fluid flow 20. The second set of multiple conduits 304 can constitute the downstream region of the nucleus boiling device 300 within the fluid flow 20. Therefore, the first group of multiple pipes 302 and the second group of multiple pipes 304 are arranged in a staggered manner, wherein the downstream region (e.g., the second group of multiple pipes 304) is higher than the upstream region (e.g., the first group of multiple pipes 302) relative to the base 306. The effect is that bubble formation in the upstream region affects bubble formation in the downstream region, and thus affects cooling, less than when the two regions are at the same level. With this design, the two flat regions where most boiling occurs become more efficient. Furthermore, the total boiling area can also be increased. Therefore, compared to existing core-shaped boiling plates 100 and 200 (respectively in…),… Figure 1 , Figure 2 (In China), the nucleus boiling device 300 can significantly improve heat transfer.
[0053] In one or more embodiments, in the first flat region 308, the surface of the first set of plurality of pipes 302 may include one or more of the aforementioned features that enhance nucleus boiling, such as microparticles or stamping recesses 320. Similarly, in one or more embodiments, in the second flat region 312, the surface of the second set of plurality of pipes 304 may include one or more of the aforementioned features that enhance nucleus boiling, such as microparticles or stamping recesses 320.
[0054] In one or more embodiments, a first group of multiple pipes 302 can be connected to a second group of multiple pipes 304 via a base 306, such that each pipe of the first group of multiple pipes 302 is connected to a corresponding pipe of the second group of multiple pipes 304 to form a single pipe. In one or more embodiments, a thermal interface material (e.g., material 318) may be present between the base 306 and the component 10.
[0055] In one or more embodiments, the first group of multiple conduits 302 may be arranged in a single layer, such as Figure 3AAs shown. In one or more embodiments, the second group of multiple conduits 304 may be arranged in a single layer, such as... Figure 3A As shown. Ideally, the first set of multiple conduits 302 and the second set of multiple conduits 304 are arranged in a single layer, with no other conduit above or below to improve nucleation. However, in one or more embodiments, the first set of multiple conduits 302 and the second set of multiple conduits 304 may be arranged in more than one layer.
[0056] The first group of multiple conduits 302 and the second group of multiple conduits 304 may include any number of conduits, depending on the amount of heat to be dissipated, the size of the base 306, etc. In one or more embodiments, the first group of multiple conduits 302 and the second group of multiple conduits 304 may each include eight conduits, such as... Figure 3B as well as Figure 3C show.
[0057] In one or more embodiments, in the first transition region 310, the first set of multiple conduits 302 are inclined relative to the base 306 in a first tilting direction at a first angle θ1. In the second transition region 314, the second set of multiple conduits 304 are inclined relative to the base 306 in a second tilting direction at a second angle θ2. In one or more embodiments, the second angle θ2 may be greater than the first angle θ1, such that the second set of multiple conduits 304 may extend to a higher horizontal plane or plane relative to the base 306 above the first set of multiple conduits 302, beyond the first set of multiple conduits 302 by a short distance.
[0058] According to the features of the present invention, Figure 3B A bottom view of the nucleo-boiling device 300 is shown. Figure 3C Showing a top view of the nucleus boiling apparatus 300. For convenience, Figures 3B to 3C The described embodiment is an example where each of the first set of multiple pipes 302 is connected to a corresponding pipe of the second set of multiple pipes 304 to form a single pipe spanning the nucleus boiling device 300. Therefore, the nucleus boiling device 300 includes eight pipes 316a to 316h. Furthermore, portions of the pipes 316a to 316h within the first flat region 308 and the second flat region 312 described above are shown fan-shaped or dispersed. This fan-shaped arrangement of the pipes 316a to 316h provides greater spacing between them, such that the nucleation effect of one pipe (e.g., 316a) on the nucleation of an adjacent pipe (e.g., 316b) is smaller compared to the case where the pipes 316a to 316h are not fan-shaped.
[0059] In one or more embodiments, the spacing between conduits 316a to 316h may be constant relative to the distance from the base 306. Alternatively, in one or more embodiments, the conduits in the first group of multiple conduits 302 in the first flat region 308, the second group of multiple conduits 304 in the second flat region 312, or both, may be spaced further apart. The distance relative to the base 306, and the distance relative to the center conduit (in... Figure 3B In the example shown, the central conduit is conduit 316d and 316e), or the spacing between conduits can be greater relative to the distance from both. Therefore, Figure 3B The distance D1 in the middle is less than Figure 3B The distance D2 is greater because pipes 316g and 316h are further from the center or midline of pipes 316a to 316h than pipes 316d and 316e, where pipes 316d and 316e roughly define the center or midline of pipes 316a to 316h. Again, this facilitates nucleation and reduces bubble binding in the outer pipes (e.g., 316a, 316b, 316g, and 316h).
[0060] As in Figure 3B as well as Figure 3C As further shown, in one or more embodiments, the cross-sectional areas of conduits 316a to 316h in the first flat region 308, the second flat region 312, or both, are greater than the cross-sectional areas of conduits 316a to 316h in the individual first transition region 310, the individual second transition region 314, or both. The larger cross-sectional areas of conduits 316a to 316h in the first flat region 308, the second flat region 312, or both provide additional surface area for nucleation.
[0061] Furthermore, in one or more embodiments, and in Figure 3B as well as Figure 3C The diagram further shows that the cross-sectional areas of conduits 316a to 316h in the first flat region 308, the second flat region 312, or both, increase relative to their distance from the base 306. This increased cross-sectional area of conduits 316a to 316h relative to their distance from the base 306 provides additional surface area for nucleation.
[0062] In one or more embodiments, and as Figure 3B as well as Figure 3CAs shown, conduits 316a to 316h are sealed hollow metal conduits. In one or more embodiments, the sealed hollow metal conduits may include a fluid, such as a working fluid. When conduits 316a to 316h are in use, the working fluid may be selected to be in a liquid or gaseous state within the conduits. In one or more embodiments, conduits 316a to 316h may be solid.
[0063] In one or more embodiments, the combined width of the first group of multiple conduits 302, the combined width of the second group of multiple conduits 304, or both, may span a width less than that of the base 306. Alternatively, the combined width of the first group of multiple conduits 302, the combined width of the second group of multiple conduits 304, or both, may span a width approximately the same as that of the base 306.
[0064] Figure 4 as well as Figure 5 The computational fluid dynamics simulation results are displayed, showing the effect of the first set of staggered pipes 302 relative to the second set of staggered pipes 304 on the base 306 of the nucleus boiling device 300. For example... Figure 4 As shown, the void fraction is generated at the first set of multiple pipes 302, and then flows and concentrates above the base 306. However, relative to the liquid flow direction, the void fraction is below the base 306 and below the second set of multiple pipes 304 downstream of the first set of multiple pipes 302. Therefore, the interference of the nucleus boiling caused by the first set of multiple pipes 302 on the nucleus boiling caused by the second set of multiple pipes 304 is less than the interference of the nucleus boiling caused by the first set of multiple pipes 302 on the nucleus boiling caused by the second set of multiple pipes 304 if the multiple pipes 302 and the multiple pipes 304 were all on the same plane or horizontal plane above the base 306.
[0065] Reference Figure 5 The staggered multiple conduits 302 and 304 provide greater heat transfer capacity to transfer heat from component 10 to the surrounding fluid. Table 1 shows that, compared to an existing core-type boiling plate (e.g., Figure 2 The nucleosurfing device 300 provides better heat dissipation than a conventional nucleosurfing plate (e.g., plate 200). The nucleosurfing device 300 can reduce thermal resistance by up to 56%. Furthermore, compared to an existing nucleosurfing plate (e.g., plate 200), the nucleosurfing device 300 offers significantly better heat dissipation. Figure 2 The plate 200 and the nucleus boiling device 300 improve heat transfer capacity by up to 80%.
[0066] project Existing design This design Thermal resistance (C / W) 0.022 0.012 degree of improvement Not applicable (N / A) 56% Power (W) 334 600 degree of improvement Not applicable (N / A) 80%
[0067] The foregoing description of the embodiments, including the illustrated embodiments, is presented for illustrative and descriptive purposes only and is not intended to exhaustively describe or limit the precise forms disclosed. Various modifications, adaptations, and uses will be apparent to those skilled in the art.
[0068] Although embodiments of the invention have been shown and described with respect to one or more implementations, equivalents and modifications will arise in those skilled in the art upon reading and understanding this specification and the accompanying drawings. Furthermore, while specific features of the invention may have been disclosed with respect to only one of several implementations, such features may be combined with one or more other features of other implementations, as may be desired and advantageous for any given or particular application.
[0069] While various embodiments of the invention have been described above, it should be understood that they are presented by way of example only and not as limiting. Various modifications may be made to the embodiments disclosed herein without departing from the spirit or scope of the invention. Therefore, the breadth and scope of the invention should not be limited by any of the foregoing embodiments. Rather, the scope of the invention should be defined by the appended claims and their equivalents.
[0070] The terminology used herein is for the purpose of describing particular embodiments only and is not intended to limit the invention. The singular forms "a" and "the" as used herein are intended to include multiple forms unless the context clearly indicates otherwise. Furthermore, the terms "including," "having," or variations thereof, as used in embodiments and / or the claims of the patent application, are intended to be included in a manner similar to the word "comprising."
[0071] Unless otherwise defined, all terms used herein (including technical and scientific terms) have the same meaning as understood by one of ordinary skill in the art. Furthermore, terms (e.g., those defined in common dictionaries) should be interpreted as having the same meaning as they have in the relevant art, and will not be interpreted herein in an idealized or overly formal sense unless explicitly defined as such.
Claims
1. A nucleus boiling device configured for use in a liquid cooling computational environment, wherein the cooling liquid flows in a flow direction, the nucleus boiling device comprising: A base, configured to be mounted on a heat-generating object to provide immersion cooling for the object in a liquid-cooled computing environment, is defined by an upper surface, a lower surface, and multiple side surfaces, including a first side surface and a second side surface. A first group of multiple conduits extends from the first side surface, the first group of multiple conduits including a first transition region and a first flat region. In the first transition region, the first group of multiple conduits extends away from the base along a first inclined direction relative to the base. In the first flat region, the first group of multiple conduits extends away from the base in a fan-shaped outward arrangement. The second group of multiple pipes extends from the second side surface. The second group of multiple pipes includes a second transition region and a second flat region. In the second transition region, the second group of multiple pipes extends away from the base along a second inclined direction relative to the base. In the second flat region, the second group of multiple pipes extends away from the base in a fan-shaped outward arrangement. The first group of multiple pipes constitutes the upstream region of the flow direction, and the second group of multiple pipes constitutes the downstream region of the flow direction. The second group of multiple pipes is arranged in a staggered manner with the first group of multiple pipes, such that the distance between the second flat region and the upper surface of the base is greater than the distance between the first flat region and the upper surface of the base.
2. The nucleus boiling device as claimed in claim 1, wherein the first group of multiple pipelines is connected to the second group of multiple pipelines through the base, such that each pipeline of the first group of multiple pipelines is connected to the corresponding pipeline of the second group of multiple pipelines to form a single pipeline.
3. The nucleus boiling device as described in claim 1, wherein the first tilting direction and the second tilting direction have different tilting angles.
4. The nucleus boiling device as claimed in claim 1, wherein in the first flat region, the cross-sectional area of each of the first group of multiple pipes is greater than the cross-sectional area in the first transition region.
5. The nucleus boiling device as claimed in claim 4, wherein in the first flat region, the cross-sectional area of each of the first group of multiple pipes increases as it moves further away from the base.
6. The nucleus boiling device as claimed in claim 4, wherein in the second flat region, the cross-sectional area of each of the second group of multiple pipes is greater than the cross-sectional area in the second transition region.
7. The nucleus boiling device as claimed in claim 6, wherein in the second flat region, the cross-sectional area of each of the second group of multiple pipes increases as it moves further away from the base.
8. The nucleus boiling device as claimed in claim 1, wherein in the first flat region, the spacing of the outer pipes of the first group of multiple pipes is greater than the spacing of the inner pipes of the first group of multiple pipes.
9. The nucleus boiling device as claimed in claim 8, wherein in the second flat region, the spacing of the outer pipes of the second group of multiple pipes is greater than the spacing of the inner pipes of the second group of multiple pipes.
10. A computing system, comprising: processor; as well as Nucleus boiling device, configured for use in a liquid cooling computing environment, wherein the cooling liquid flows in the flow direction, the nucleus boiling device has The base is defined by an upper surface, a lower surface, and multiple side surfaces, including a first side surface and a second side surface, and the lower surface is in contact with or close to the processor. A first group of multiple pipes extends from the first side surface. The first group of multiple pipes includes a first transition region and a first flat region. In the first transition region, the first group of multiple pipes extends away from the base along a first inclined direction relative to the base. In the first flat region, the first group of multiple pipes extends outward in a first fan shape perpendicular to the first side surface. as well as The second group of multiple pipes extends from the second side surface. The second group of multiple pipes includes a second transition region and a second flat region. In the second transition region, the second group of multiple pipes extends away from the base along a second inclined direction relative to the base. In the second flat region, the second group of multiple pipes extends outward in a second fan shape perpendicular to the second side surface. The first group of multiple pipes constitutes the upstream region of the flow direction, and the second group of multiple pipes constitutes the downstream region of the flow direction. The second group of multiple pipes is arranged in a staggered manner with the first group of multiple pipes, such that the distance between the second flat region and the upper surface of the base is greater than the distance between the first flat region and the upper surface of the base.