CN214426510U - Ultrathin heat pipe capable of efficiently exchanging heat - Google Patents
Ultrathin heat pipe capable of efficiently exchanging heat Download PDFInfo
- Publication number
- CN214426510U CN214426510U CN202120316529.XU CN202120316529U CN214426510U CN 214426510 U CN214426510 U CN 214426510U CN 202120316529 U CN202120316529 U CN 202120316529U CN 214426510 U CN214426510 U CN 214426510U
- Authority
- CN
- China
- Prior art keywords
- evaporation
- condensation
- section
- hydrophobic
- hydrophilic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)
Abstract
The utility model provides an ultrathin heat pipe with high heat exchange efficiency, which comprises an evaporation section, a heat insulation section and a condensation section which are connected in sequence; the evaporation section comprises an evaporation pipe body and an evaporation liquid absorption core; a plurality of hydrophobic micro-nano small holes are distributed in the evaporation liquid absorption core; the inner wall of the evaporation tube body is provided with a cavity; the wall and the edge of each hydrophobic micro-nano small hole and the surface of the cavity are covered with a hydrophobic film; the surface of the hydrophobic film is uniformly and densely distributed with super-hydrophobic nucleation pits; the condensation section comprises a condensation pipe body and a condensation liquid absorption core; the condensation liquid absorption core is provided with a plurality of hydrophilic micro-nano small holes; the wall and the edge of each hydrophilic micro-nano pore and the inner wall of the condensation pipe body are covered with a hydrophilic film; the surface of the hydrophilic film is uniformly and densely distributed with super-hydrophilic nucleation convex points; and end covers are respectively arranged at one end of the evaporation section, which is far away from the heat insulation section, and one end of the condensation section, which is far away from the heat insulation section. The heat pipe improves the heat exchange performance by improving the phase change heat exchange capacity, realizes light weight and compactness, and is convenient for the injection and the replacement of the working medium.
Description
Technical Field
The utility model relates to a heat dissipation device technical field, more specifically say, relate to an ultra-thin heat pipe of high-efficient heat transfer.
Background
The LSI technology is the core of intelligent manufacturing and is also the key toggle for upgrading other manufacturing industries. The heat dissipation problem is a bottleneck which needs to be solved urgently in the electronic chip industry, the reliability of an electronic product can be reduced to half of the original reliability when the temperature of the electronic product rises by 10 ℃ sharply, and the reliability of the electronic product is changed to 20% of the original reliability when the temperature rises from 75 ℃ to 125 ℃. Along with the improvement of the integration level of electronic chips, the functions of integrated devices become more complex, the power is increased continuously, and in addition, the requirements of miniaturization and mobility of electronic equipment in special fields are added, the structural design of the integrated device develops towards the direction of small-sized assembly, the heat flux density on a unit area approaches the critical of various existing cooling measures, the surface heating distribution of microelectronic chips is uneven, and the local heat flux intensity can reach 1000W/cm2Therefore, the limit of the existing cooling technology needs to be broken through, and the development of more efficient and compact heat dissipation technology for electronic components is urgent.
The micro heat pipe phase change heat transfer is the most effective method for solving the problem of heat control of a chip with high heat flow density in a narrow space. The heat pipe technology is a heat transfer element which is invented by the United states Ross Alamous national laboratory in 1963 and efficiently conducts heat by utilizing the phase change principle, and the heat conduction coefficient can reach more than 20000W/m. The micro heat pipe consists of a wall shell, a liquid absorption core and a working medium. One end of the micro heat pipe is evaporated, the other end of the micro heat pipe is condensed, when one end of the micro heat pipe is heated, the working medium absorbs heat and is vaporized and flows to the other end of the wall shell to release heat at a speed close to the sound velocity under the condition of high vacuum, and condensed liquid flows back to the evaporation end along the porous material by virtue of the capillary action. The heat pipe technology fully utilizes the heat conduction principle and the rapid heat transfer property of the phase change medium, heat of a heating object is rapidly transferred to the outside of a heat source through the heat pipe, and the heat conduction capability of the heat pipe exceeds the heat conduction capability of any known solid, so the heat pipe technology is widely applied to the industries of aerospace, military industry, computer CPU heat dissipation and the like. In 2013, the Japan NEC company adopts a phase-change heat-transfer micro heat pipe (the thickness is 0.6mm, the heat conductivity coefficient is about ten times of that of a graphite sheet and is one hundred times of that of a copper/aluminum material) for the first time to radiate heat of the smart phone, and a good effect is achieved.
The development in the field of electronic chips puts very strict requirements on the processing of micro heat pipes. For example, the thickness of a conventional heat pipe is generally more than 2.0 mm. However, the current requirements of various internet devices on the thickness of the micro heat pipe reach 0.4-0.6mm, and the heat transfer power within 3 ℃ temperature difference is required to be not less than 3W, but the current micro heat pipe is difficult to achieve the performance level.
The performance of the micro heat pipe is improved depending on the size of the heat exchange capacity, which is closely related to the phase change ends at the two ends. How to boil the evaporation end with high efficiency and how to condense beads at the condensation end is a breakthrough for improving the performance of the heat pipe. Due to the limited space and the complex competition of evaporation and condensation, various boiling and condensation enhanced heat exchange technologies in the conventional large-scale heat exchange equipment are difficult to directly transplant into the micro heat pipe. Therefore, it is necessary to design a heat pipe capable of further improving the heat exchange capability.
SUMMERY OF THE UTILITY MODEL
For overcoming shortcoming and not enough among the prior art, the utility model aims to provide an ultra-thin heat pipe that has bionical imbibition core, promotes heat transfer performance, realizes lightweight and compactification, the working medium of being convenient for pours into and changes into through promoting phase transition heat transfer ability.
In order to achieve the above purpose, the utility model discloses a following technical scheme realizes: the utility model provides an ultra-thin heat pipe of high-efficient heat transfer which characterized in that: comprises an evaporation section, a heat insulation section and a condensation section which are connected in sequence;
the evaporation section comprises an evaporation pipe body and an evaporation liquid absorption core; the evaporation liquid absorption core is arranged in the tube cavity of the evaporation tube body, and a gap is formed between the evaporation liquid absorption core and the inner wall of the evaporation tube body to form an outer evaporation flow channel; the evaporation liquid absorption core is provided with an inner evaporation flow passage; the evaporation liquid absorption core is provided with a plurality of hydrophobic micro-nano small holes which are communicated with the outer evaporation flow channel and the inner evaporation flow channel; a cavity is formed in the inner wall of the evaporation tube body at the position opposite to the hydrophobic micro-nano small hole; the wall and the edge of each hydrophobic micro-nano small hole and the surface of the cavity are covered with a hydrophobic film; the surface of the hydrophobic membrane is uniformly and densely distributed with super-hydrophobic nucleation pits, the pit walls and edges of the super-hydrophobic nucleation pits are super-hydrophobic surfaces, and the rest areas of the surface of the hydrophobic membrane are super-hydrophilic surfaces;
the condensation section comprises a condensation pipe body and a condensation liquid suction core; the condensation liquid absorption core is arranged in the pipe cavity of the condensation pipe body, and a gap is formed between the condensation liquid absorption core and the inner wall of the condensation pipe body to form an outer condensation flow channel; the condensation liquid absorption core is provided with an internal condensation flow passage; the condensation liquid absorption core is provided with a plurality of hydrophilic micro-nano holes which are communicated with the outer condensation flow channel and the inner condensation flow channel; the wall and the edge of each hydrophilic micro-nano pore and the inner wall of the condensation pipe body are covered with a hydrophilic film; the surfaces of the hydrophilic membranes are uniformly and densely distributed with super-hydrophilic nucleation convex points, the surfaces and edges of the super-hydrophilic nucleation convex points are super-hydrophilic surfaces, and the rest areas of the surfaces of the hydrophilic membranes are super-hydrophobic surfaces;
the outer evaporation flow channel, the inner evaporation flow channel, the outer condensation flow channel and the inner condensation flow channel are all communicated with the heat insulation section to form a circulation loop of the outer evaporation flow channel, the inner evaporation flow channel, the heat insulation section, the inner condensation flow channel and the outer condensation flow channel; and end covers are respectively arranged at one end of the evaporation section, which is far away from the heat insulation section, and one end of the condensation section, which is far away from the heat insulation section.
The working principle of the heat pipe of the utility model is that: in an evaporation section of the heat pipe, a working medium is boiled, bubble nucleation is accelerated under the hydrophobic action of a super-hydrophobic nucleation pit, bubble separation is accelerated under the hydrophilic action of a super-hydrophilic surface after bubble nucleation, and a large number of bubbles are formed to finish efficient boiling heat exchange; at the condensation segment of heat pipe, the bubble is under the hydrophilic effect of super hydrophilic nucleation salient point with higher speed the liquid drop nucleation, and the hydrophobic effect on super hydrophobic surface more is favorable to the pearl to condense at the liquid drop in-process of growing up, and the reinforcing condensation heat transfer avoids producing thick liquid film to accomplish high-efficient heat dissipation.
The utility model discloses strengthen phase transition heat transfer based on moist regulation and control and promote the heat transfer performance of heat pipe, hydrophobic membrane and hydrophilic membrane all have super hydrophilic surface and super hydrophobic surface simultaneously, satisfy the different demands of phase transition to surface wettability in different stages; through the promotion of phase change heat transfer ability, realize the technological breakthrough of heat pipe lightweight, compactification, be applicable to the heat dissipation application of products such as electronic chip, small-size electron device. The end cover is adopted for heat pipe sealing, so that the working medium can be conveniently injected and replaced.
Preferably, the cavity is in the shape of an inverted cone.
Preferably, the hydrophobic membrane positioned at the edge of the hydrophobic micro-nano small hole comprises an outer hydrophobic membrane close to one side of the tube wall of the evaporation tube body and an inner hydrophobic membrane far away from one side of the tube wall of the evaporation tube body; the hydrophobic membrane positioned on the surface of the cavity is a cavity hydrophobic membrane; the outer diameter of the inner hydrophobic membrane is larger than the outer diameter of the outer hydrophobic membrane and larger than the outer diameter of the cavity hydrophobic membrane.
Preferably, the hydrophilic film positioned at the edge of the hydrophilic micro-nano small hole comprises an outer hydrophilic film close to one side of the pipe wall of the condensation pipe body and an inner hydrophilic film far away from one side of the pipe wall of the condensation pipe body; the outer diameter of the inner hydrophilic film is less than that of the outer hydrophilic film.
The outer diameter of the inner hydrophobic membrane is larger than that of the outer hydrophobic membrane and larger than that of the cavity hydrophobic membrane, and the capillary acting force is gradually decreased layer by layer, so that bubbles can be discharged; the outer diameter of the inner hydrophilic film is smaller than that of the outer hydrophilic film, and the capillary force increases gradually layer by layer, which is beneficial to discharging liquid drops.
Preferably, the heat insulation section adopts a through groove structure; and liquid working medium is collected from the condensation section by utilizing capillary force and is supplied to the evaporation section.
Preferably, the through trench structure is: the inner wall of the heat insulation section is provided with a plurality of clapboards which respectively extend along the length direction of the heat pipe, and a groove with capillary force is reserved between the adjacent clapboards.
Preferably, the number of the evaporation section, the heat insulation section and the condensation section is one or more than two respectively;
when more than two evaporation sections are arranged, all the evaporation sections are connected in sequence and then connected with the heat insulation section;
when the number of the heat insulation sections is more than two, all the heat insulation sections are connected in sequence and then are respectively connected with the evaporation section and the condensation section;
when the number of the condensing sections is more than two, all the condensing sections are connected in sequence and then connected with the heat insulation section.
The design can realize the modular design and assembly of the evaporation section, the heat insulation section and the condensation section, improve the universality of the heat pipe and save the production cost.
Preferably, the evaporation section, the heat insulation section and the condensation section are connected in a plug-in manner; can adopt the mode of building blocks of similar happy height to realize pegging graft, the equipment is simple convenient.
Compared with the prior art, the utility model has the advantages of as follows and beneficial effect:
1. the utility model discloses strengthen phase transition heat transfer based on moist regulation and control and promote the heat transfer performance of heat pipe, hydrophobic membrane and hydrophilic membrane all have super hydrophilic surface and super hydrophobic surface simultaneously, satisfy the different demands of phase transition to surface wettability in different stages; through the improvement of the phase-change heat exchange capacity, the technical breakthrough of light weight and compactness of the heat pipe is realized, and the heat pipe is suitable for heat dissipation application of products such as electronic chips, small-sized electronic devices and the like;
2. in the evaporation section of the utility model, the outer diameter of the inner hydrophobic membrane is larger than the outer diameter of the outer hydrophobic membrane and larger than the outer diameter of the cavity hydrophobic membrane, and the capillary force is gradually decreased layer by layer, thus being beneficial to discharging bubbles; in the condensation section, the outer diameter of the inner hydrophilic film is smaller than that of the outer hydrophilic film, and the capillary force is gradually increased layer by layer, so that liquid drops are discharged; the heat exchange efficiency can be further accelerated;
3. the utility model can realize modular design and assembly, improve the universality of the heat pipe and save the production cost; the assembly is simple and convenient.
Drawings
FIG. 1 is a schematic structural view of an ultra-thin heat pipe for efficient heat exchange according to the present invention;
FIG. 2 is a schematic view of the flow direction of the working medium of the ultra-thin heat pipe for efficient heat exchange of the present invention;
FIG. 3 is an enlarged view of portion B of FIG. 1;
FIG. 4 is an enlarged view of portion C of FIG. 1;
FIG. 5 is a cross-sectional view taken along line A-A of FIG. 1;
FIG. 6 is a schematic diagram of bubble nucleation on the hydrophobic membrane of the ultra-thin heat pipe with high heat exchange efficiency of the present invention;
FIG. 7 is a schematic view of nucleation of liquid droplets on the hydrophilic membrane of the ultra-thin heat pipe with high heat exchange efficiency of the present invention;
the device comprises an evaporation section 1, an evaporation tube body 11, an evaporation wick 12, a hydrophobic micro-nano pore 13, a cavity 14, a hydrophobic membrane 15, a super-hydrophobic nucleation pit 151, a super-hydrophobic surface 152, a super-hydrophilic surface 153, a thermal insulation section 2, a partition plate 21, a condensation section 3, a condensation tube body 31, a condensation wick 32, a hydrophilic micro-nano pore 33, a hydrophilic membrane 34, a super-hydrophilic nucleation convex point 341, a super-hydrophilic surface 342, a super-hydrophobic surface 343, an end cover 4, a liquid working medium 51, a bubble 52, a steam working medium 53 and a droplet working medium 54.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
Example one
As shown in fig. 1 to 7, the ultrathin heat pipe for efficient heat exchange of the present embodiment includes an evaporation section 1, a heat insulation section 2, and a condensation section 3, which are connected in sequence.
The evaporation section 1 comprises an evaporation pipe body 11 and an evaporation wick 12; the evaporation wick 12 is arranged in the tube cavity of the evaporation tube body 11 and has a gap with the inner wall of the evaporation tube body 11 to form an outer evaporation flow channel; the evaporation wick 12 is provided with an inner evaporation flow channel; the evaporation liquid absorption core 12 is provided with a plurality of hydrophobic micro-nano small holes 13 which are communicated with the outer evaporation flow channel and the inner evaporation flow channel. A cavity 14 is formed in the inner wall of the evaporation tube body 11 at the position opposite to the hydrophobic micro-nano small hole 13; the cavity 14 is of an inverted conical shape. The hole wall and the edge of each hydrophobic micro-nano small hole 13 and the surface of the cavity 14 are covered with a hydrophobic film 15; the super-hydrophobic nucleation pits 151 are uniformly and densely distributed on the surface of the hydrophobic film 15, and the super-hydrophobic nucleation pits 151 are in an inverted cone shape. The walls and edges of the super-hydrophobic nucleation pits 151 are super-hydrophobic surfaces 152, and the rest areas of the surfaces of the hydrophobic membranes 15 are super-hydrophilic surfaces 153.
The hydrophobic membrane 15 positioned at the edge of the hydrophobic micro-nano small hole 13 comprises an outer hydrophobic membrane close to one side of the tube wall of the evaporation tube body 11 and an inner hydrophobic membrane far away from one side of the tube wall of the evaporation tube body 11; the hydrophobic film 15 on the surface of the cavity 14 is a cavity hydrophobic film; the inner hydrophobic membrane outer diameter D1 > the outer hydrophobic membrane outer diameter D2 > the cavity hydrophobic membrane outer diameter D3.
The condensation section 3 comprises a condensation pipe body 31 and a condensation wick 32; the condensation wick 32 is arranged in the pipe cavity of the condensation pipe body 31 and has a gap with the inner wall of the condensation pipe body 31 to form an outer condensation flow passage; the condensation wick 32 is provided with an internal condensation flow passage; the condensation liquid absorption core 32 is provided with a plurality of hydrophilic micro-nano holes 33 which are communicated with the outer condensation flow channel and the inner condensation flow channel; the hole wall and the edge of each hydrophilic micro-nano pore 33 and the inner wall of the condensation pipe body 31 are covered with a hydrophilic film 34; the super-hydrophilic nucleation convex points 341 are uniformly and densely distributed on the surface of the hydrophilic film 34, and the super-hydrophilic nucleation convex points 341 are cylindrical. The surfaces and edges of the super-hydrophilic nucleation convex points 341 are super-hydrophilic surfaces 342, and the rest areas on the surface of the hydrophilic membrane 34 are super-hydrophobic surfaces 343.
The hydrophilic film 34 positioned at the edge of the hydrophilic micro-nano small hole 33 comprises an outer hydrophilic film close to one side of the pipe wall of the condensation pipe body 31 and an inner hydrophilic film far away from one side of the pipe wall of the condensation pipe body 31; the inner hydrophilic film outer diameter D4 < the outer hydrophilic film outer diameter D5.
The outer evaporation flow passage, the inner evaporation flow passage, the outer condensation flow passage and the inner condensation flow passage are all communicated with the heat insulation section 2 to form a circulation loop of the outer evaporation flow passage, the inner evaporation flow passage, the heat insulation section 2, the inner condensation flow passage and the outer condensation flow passage.
The working principle of the heat pipe of the utility model is that: in the evaporation section 1 of the heat pipe, the working medium is boiled, the nucleation of bubbles is accelerated under the hydrophobic action of the super-hydrophobic nucleation pit 151, the separation of the bubbles is accelerated under the hydrophilic action of the super-hydrophilic surface after the nucleation of the bubbles, and a large number of bubbles are formed to finish efficient boiling heat exchange; at condensation segment 3 of heat pipe, the bubble is under the hydrophilic effect of super hydrophilic nucleation salient 341 with higher speed the liquid drop nucleation, and the hydrophobic effect on super hydrophobic surface more is favorable to the pearl to condense at the liquid drop in-process of growing up, and the reinforcing condensation heat transfer avoids producing thick liquid film to accomplish high-efficient heat dissipation.
The utility model discloses strengthen the phase transition heat transfer based on moist regulation and control and promote the heat transfer performance of heat pipe, hydrophobic membrane 15 and hydrophilic membrane 34 have super hydrophilic surface and super hydrophobic surface concurrently, satisfy the different demands of phase transition to surface wettability in different stages; through the promotion of phase change heat transfer ability, realize the technological breakthrough of heat pipe lightweight, compactification, be applicable to the heat dissipation application of products such as electronic chip, small-size electron device.
The outer diameter D1 of the inner hydrophobic membrane is larger than the outer diameter D2 of the outer hydrophobic membrane is larger than the outer diameter D3 of the cavity hydrophobic membrane, and the capillary force decreases gradually layer by layer, so that bubbles can be discharged; the outer diameter D4 of the inner hydrophilic film is less than the outer diameter D5 of the outer hydrophilic film, and the capillary force is gradually increased layer by layer, which is beneficial to discharging liquid drops.
The preferred method for making the hydrophobic membrane 15 and the hydrophilic membrane 34 is: the hydrophobic membrane 15 is formed by connecting the evaporation tube body 11/evaporation wick 12 with the positive electrode of a high-pulse power supply, spraying a nozzle with hydrophobic nano-materials and hydrophilic nano-materials on the evaporation tube body 11/evaporation wick 12, and attracting the hydrophobic nano-materials and the hydrophilic nano-materials to be deposited on the evaporation tube body 11/evaporation wick 12 by utilizing the electrostatic induction effect.
The hydrophilic membrane 34 is a hydrophilic membrane 34 formed by connecting the condensation pipe body 31/condensation wick 32 with the positive electrode of a high-pulse power supply, spraying a nozzle with a hydrophobic nano material and a hydrophilic nano material on the condensation pipe body 31/condensation wick 32, and attracting the hydrophobic nano material and the hydrophilic nano material to deposit on the condensation pipe body 31/condensation wick 32 by utilizing the electrostatic induction.
The manufacturing method sprays corresponding nano materials at the designed positions, has simpler process, and is beneficial to improving the process precision, thereby ensuring that the internal structure size of the heat pipe has good precision.
The evaporation section 1, the heat insulation section 2 and the condensation section 3 are connected in a plug-in mode; can adopt the mode of building blocks of similar happy height to realize pegging graft, easy operation is convenient.
And one end of the evaporation section 1, which is far away from the heat insulation section 2, and one end of the condensation section 3, which is far away from the heat insulation section 2, are respectively provided with an end cover 4, so that the internal sealing of the heat pipe is realized, and the working medium is conveniently injected and replaced.
The heat insulation section 2 adopts a through type groove structure; liquid working medium is collected from the condensation section 3 by utilizing capillary force and is supplied to the evaporation section 1. The through trench structure is: the inner wall of the heat insulation section 2 is provided with a plurality of clapboards 21 which respectively extend along the length direction of the heat pipe, and grooves with capillary force are reserved between the adjacent clapboards 21.
Example two
The embodiment is an ultrathin heat pipe with high-efficiency heat exchange, and the difference from the embodiment I is that: in the first embodiment, the number of the evaporation section, the heat insulation section and the condensation section is one. In the embodiment, the number of the evaporation sections and/or the heat insulation sections and/or the condensation sections is more than two;
when more than two evaporation sections are arranged, all the evaporation sections are connected in sequence and then connected with the heat insulation section;
when the number of the heat insulation sections is more than two, all the heat insulation sections are connected in sequence and then are respectively connected with the evaporation section and the condensation section;
when the number of the condensing sections is more than two, all the condensing sections are connected in sequence and then connected with the heat insulation section.
The design can realize the modular design and assembly of the evaporation section, the heat insulation section and the condensation section, improve the universality of the heat pipe and save the production cost.
The rest of the structure of the present embodiment is the same as that of the first embodiment.
The above embodiments are preferred embodiments of the present invention, but the embodiments of the present invention are not limited to the above embodiments, and any other changes, modifications, substitutions, combinations, and simplifications which do not depart from the spirit and principle of the present invention should be equivalent replacement modes, and all are included in the scope of the present invention.
Claims (8)
1. The utility model provides an ultra-thin heat pipe of high-efficient heat transfer which characterized in that: comprises an evaporation section, a heat insulation section and a condensation section which are connected in sequence;
the evaporation section comprises an evaporation pipe body and an evaporation liquid absorption core; the evaporation liquid absorption core is arranged in the tube cavity of the evaporation tube body, and a gap is formed between the evaporation liquid absorption core and the inner wall of the evaporation tube body to form an outer evaporation flow channel; the evaporation liquid absorption core is provided with an inner evaporation flow passage; the evaporation liquid absorption core is provided with a plurality of hydrophobic micro-nano small holes which are communicated with the outer evaporation flow channel and the inner evaporation flow channel; a cavity is formed in the inner wall of the evaporation tube body at the position opposite to the hydrophobic micro-nano small hole; the wall and the edge of each hydrophobic micro-nano small hole and the surface of the cavity are covered with a hydrophobic film; the surface of the hydrophobic membrane is uniformly and densely distributed with super-hydrophobic nucleation pits, the pit walls and edges of the super-hydrophobic nucleation pits are super-hydrophobic surfaces, and the rest areas of the surface of the hydrophobic membrane are super-hydrophilic surfaces;
the condensation section comprises a condensation pipe body and a condensation liquid suction core; the condensation liquid absorption core is arranged in the pipe cavity of the condensation pipe body, and a gap is formed between the condensation liquid absorption core and the inner wall of the condensation pipe body to form an outer condensation flow channel; the condensation liquid absorption core is provided with an internal condensation flow passage; the condensation liquid absorption core is provided with a plurality of hydrophilic micro-nano holes which are communicated with the outer condensation flow channel and the inner condensation flow channel; the wall and the edge of each hydrophilic micro-nano pore and the inner wall of the condensation pipe body are covered with a hydrophilic film; the surfaces of the hydrophilic membranes are uniformly and densely distributed with super-hydrophilic nucleation convex points, the surfaces and edges of the super-hydrophilic nucleation convex points are super-hydrophilic surfaces, and the rest areas of the surfaces of the hydrophilic membranes are super-hydrophobic surfaces;
the outer evaporation flow channel, the inner evaporation flow channel, the outer condensation flow channel and the inner condensation flow channel are all communicated with the heat insulation section to form a circulation loop of the outer evaporation flow channel, the inner evaporation flow channel, the heat insulation section, the inner condensation flow channel and the outer condensation flow channel; and end covers are respectively arranged at one end of the evaporation section, which is far away from the heat insulation section, and one end of the condensation section, which is far away from the heat insulation section.
2. The ultra-thin heat pipe with high heat exchange efficiency as claimed in claim 1, wherein: the cavity is in an inverted cone shape.
3. The ultra-thin heat pipe with high heat exchange efficiency as claimed in claim 1, wherein: the hydrophobic membrane positioned at the edge of the hydrophobic micro-nano small hole comprises an outer hydrophobic membrane close to one side of the tube wall of the evaporation tube body and an inner hydrophobic membrane far away from one side of the tube wall of the evaporation tube body; the hydrophobic membrane positioned on the surface of the cavity is a cavity hydrophobic membrane; the outer diameter of the inner hydrophobic membrane is larger than the outer diameter of the outer hydrophobic membrane and larger than the outer diameter of the cavity hydrophobic membrane.
4. The ultra-thin heat pipe with high heat exchange efficiency as claimed in claim 1, wherein: the hydrophilic film positioned at the edge of the hydrophilic micro-nano small hole comprises an outer hydrophilic film close to one side of the pipe wall of the condensation pipe body and an inner hydrophilic film far away from one side of the pipe wall of the condensation pipe body; the outer diameter of the inner hydrophilic film is less than that of the outer hydrophilic film.
5. The ultra-thin heat pipe with high heat exchange efficiency as claimed in claim 1, wherein: the heat insulation section adopts a through type groove structure.
6. The ultrathin heat pipe with high heat exchange efficiency as claimed in claim 5, characterized in that: the penetrating type groove structure is as follows: the inner wall of the heat insulation section is provided with a plurality of clapboards which respectively extend along the length direction of the heat pipe, and a groove with capillary force is reserved between the adjacent clapboards.
7. The ultrathin heat pipe for efficient heat exchange according to any one of claims 1 to 6, wherein: the number of the evaporation section, the heat insulation section and the condensation section is respectively one or more than two;
when more than two evaporation sections are arranged, all the evaporation sections are connected in sequence and then connected with the heat insulation section;
when the number of the heat insulation sections is more than two, all the heat insulation sections are connected in sequence and then are respectively connected with the evaporation section and the condensation section;
when the number of the condensing sections is more than two, all the condensing sections are connected in sequence and then connected with the heat insulation section.
8. The ultrathin heat pipe for efficient heat exchange according to any one of claims 1 to 6, wherein: the evaporation section, the heat insulation section and the condensation section are connected in a plug-in mode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120316529.XU CN214426510U (en) | 2021-02-04 | 2021-02-04 | Ultrathin heat pipe capable of efficiently exchanging heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120316529.XU CN214426510U (en) | 2021-02-04 | 2021-02-04 | Ultrathin heat pipe capable of efficiently exchanging heat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214426510U true CN214426510U (en) | 2021-10-19 |
Family
ID=78071482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120316529.XU Active CN214426510U (en) | 2021-02-04 | 2021-02-04 | Ultrathin heat pipe capable of efficiently exchanging heat |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214426510U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114322617A (en) * | 2022-02-15 | 2022-04-12 | 上海豪承信息技术有限公司 | Heat pipe for enhancing heat transfer |
| TWI840992B (en) * | 2022-04-21 | 2024-05-01 | 廣達電腦股份有限公司 | Boiling plate and computing system |
-
2021
- 2021-02-04 CN CN202120316529.XU patent/CN214426510U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114322617A (en) * | 2022-02-15 | 2022-04-12 | 上海豪承信息技术有限公司 | Heat pipe for enhancing heat transfer |
| TWI840992B (en) * | 2022-04-21 | 2024-05-01 | 廣達電腦股份有限公司 | Boiling plate and computing system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108444324B (en) | Soaking plate | |
| CN214426510U (en) | Ultrathin heat pipe capable of efficiently exchanging heat | |
| WO2022033289A1 (en) | Flat plate heat pipe and manufacturing method therefor, and heat exchanger | |
| CN104634148B (en) | A kind of nanostructured flat-plate heat pipe | |
| CN110610911B (en) | Novel three-dimensional uniform distribution manifold type microchannel | |
| CN106604607B (en) | A kind of no liquid-sucking core ultrathin heat pipe device | |
| CN1639532A (en) | Capillary evaporator | |
| CN107167008A (en) | A kind of ultra-thin panel heat pipe and its manufacture method | |
| CN110763062B (en) | Heat conduction and heat dissipation integrated flat heat pipe | |
| CN1781007A (en) | Cooling device of thin plate type for preventing dry-out | |
| CN208779995U (en) | A kind of soaking plate | |
| CN114025562B (en) | Soaking plate with gradient liquid suction core structure and preparation method thereof | |
| CN1873360A (en) | Ring type heat exchanging system | |
| CN112781421B (en) | Ultrathin heat pipe with bionic liquid absorption core | |
| CN111380389A (en) | Vapor chamber | |
| CN112113450A (en) | Oscillation composite capillary core soaking plate structure for aerospace electronic heat dissipation | |
| CN114577044B (en) | Micro-flat heat pipe with electrohydrodynamic action | |
| CN211012603U (en) | Ultrathin flexible flat heat pipe | |
| Chen et al. | Enhanced boiling heat transfer performance on mini-pin-finned copper surfaces in FC-72 | |
| Zhang et al. | Experimental study on the characteristics of loop heat pipe with modified carbon fiber felt wick | |
| CN113053840B (en) | Bionic double-loop three-dimensional micro-channel heat dissipation device | |
| CN1485905A (en) | Heat transmission device and method for production thereof | |
| Tang et al. | Pool boiling heat transfer performance of micro-embossing molds for the fabrication of polymer wicks | |
| CN113915594A (en) | Radiator with double-phase change cavity | |
| CN108418545A (en) | A kind of micro jet flow coldplate and its manufacturing method that porous heating surface is added |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |