Blow-up plate heat exchanger
By arranging circular structural partitions made of pure aluminum in the heat transfer area of the blown plate heat exchanger to form refrigerant flow channels, the problem of insufficient flow channel distribution is solved and uniform distribution and temperature uniformity of refrigerant are achieved. Improved heat exchange efficiency and cooling effect.
Patent Information
- Application Number
- CN202421175869.5
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-05-27
- Publication Date
- 2025-01-24
- Estimated Expiration
- 2034-05-27
AI Technical Summary
Due to insufficient flow channel distribution in the existing inflation plate heat exchangers, the heat exchange efficiency and temperature uniformity are poor, and the refrigerant is insufficient to bear sufficient pressure, making it impossible to transfer heat effectively.
A circular structural partition made of pure aluminum is set up in the heat transfer area to form a refrigerant flow channel, and the flow channel is made using an inflation process to ensure that the distance between the flow channels is between 4.1 and 5.2mm, forming an L-shaped structure The main body of the inflatable plate.
It achieves uniform distribution of refrigerant and uniform temperature, improves heat exchange efficiency, meets the pressure requirements of most refrigerants, and ensures refrigeration effect.
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Figure CN222393407U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of heat exchangers, in particular to a blowing plate heat exchanger. Background Art
[0002] The inflatable heat spreader is a new type of two-phase heat dissipation product. It has no capillary structure inside and is processed by printing, hot rolling, cold rolling, inflating and other processes. The refrigerant evaporates and condenses continuously in the plate with a specific circuit channel, relying on the phase change of the working fluid to efficiently transfer heat. It originated from the refrigerator evaporator and heat pump evaporator. The main technical points include refrigerant design, pipeline optimization and pressure design.
[0003] The disadvantage of the existing technology is that the heat exchange of the blown plate heat exchanger requires internal flow channels to provide heat, and the distribution of the flow channels determines the heat exchange efficiency and the heat exchange area. However, the flow channels cannot be increased indefinitely, because the size, thickness, and dimensions of the flow channels determine the internal pressure limit that the blown plate itself can withstand, and cannot be infinitely large. Since the refrigerant is generally used inside, and the pressure of the refrigerant increases with the increase of temperature, if it cannot withstand a large pressure, the refrigerant cannot flow inside. Utility Model Content
[0004] In view of the defects in the prior art, the purpose of the utility model is to provide a blowing plate heat exchanger.
[0005] The technical solution adopted by the utility model is:
[0006] A blowing plate heat exchanger comprises a blowing plate body, wherein a heat transfer area is provided in the blowing plate body, a refrigerant filling port is provided on one side of the heat transfer area, a plurality of partitions are arranged in the heat transfer area at intervals, the partitions are circular structures made of pure aluminum, and the intervals between the partitions form a refrigerant flow channel.
[0007] Furthermore, the distance of the refrigerant flow channel is 4.1 to 5.2 mm.
[0008] Furthermore, the partitions are arranged in a rectangular array.
[0009] Furthermore, the edge of the heat transfer zone is a wavy structure.
[0010] Furthermore, the refrigerant flow channel is manufactured by a blowing process.
[0011] Furthermore, the blowing plate body and the heat transfer zone are both L-shaped structures.
[0012] Furthermore, the blowing plate body includes a first side, a second side, a third side, a fourth side and a fifth side, the second side and the third side are opposite to the first side, and the fourth side and the fifth side are adjacent to the first side; the length of the first side is 750 mm, the length of the second side is 400 mm, the length of the third side is 350 mm, the length of the fourth side is 450 mm, and the length of the fifth side is 150 mm.
[0013] Additional aspects and advantages of the present application will be given in part in the description below, and in part will become apparent from the description below, or will be learned through the practice of the present application. BRIEF DESCRIPTION OF THE DRAWINGS
[0014] In order to more clearly illustrate the specific implementation of the utility model or the technical solution in the prior art, the following is a brief introduction to the drawings required for the specific implementation or the prior art description. In all the drawings, similar elements or parts are generally identified by similar reference numerals. In the drawings, each element or part is not necessarily drawn according to the actual scale.
[0015] Figure 1 A schematic diagram of the structure of a blown plate heat exchanger provided in an embodiment of the present application.
[0016] Among them, there are a blowing plate body 1, a heat transfer area 2, a partition 3, a refrigerant flow channel 4, and a refrigerant filling port 5. DETAILED DESCRIPTION
[0017] Here, it should be noted that the functions and methods involved in the present invention are merely conventional adaptive applications of the prior art. Therefore, the improvement of the present invention on the prior art is essentially the connection relationship between the hardware, rather than the functions and methods themselves. That is, although the present invention involves some functions and methods, it does not include improvements to the functions and methods themselves. The description of the functions and methods in the present invention is to better illustrate the present invention so as to better understand the present invention.
[0018] The following embodiments of the technical solution of the utility model are described in detail in conjunction with the accompanying drawings. The following embodiments are only used to more clearly illustrate the technical solution of the utility model, and are therefore only used as examples, and cannot be used to limit the protection scope of the utility model.
[0019] It should be noted that, unless otherwise specified, the technical terms or scientific terms used in this application should have the common meanings understood by technicians in the field to which the utility model belongs.
[0020] See also Figure 1The present application discloses a blown plate heat exchanger, comprising a blown plate body 1, wherein the blown plate body 1 has a heat transfer area 2, wherein a refrigerant filling port 5 is disposed on one side of the heat transfer area 2, wherein a plurality of partitions 3 are provided at intervals in the heat transfer area 2, wherein the partitions 3 are circular structures made of pure aluminum, and the intervals between the partitions 3 form a refrigerant flow channel 4.
[0021] The present application sets a circular structure partition 3 made of pure aluminum in the heat transfer zone 2, and forms a refrigerant flow channel 4 between the partitions 3. With this structure, the entire heat transfer zone 2 is evenly covered with the refrigerant flow channel 4. The refrigerant can be poured into the heat transfer zone 2 through the refrigerant filling port 5 and flow in the refrigerant flow channel 4. The refrigerant can spread over the entire heat transfer zone 2 through the refrigerant flow channel 4, so that the temperature of the entire heat transfer zone 2 is uniform, which solves the problem of uneven temperature of the blowing plate caused by the refrigerant not being able to cover the flow channel.
[0022] The blowing plate body 1 and the heat transfer zone 2 are both L-shaped structures. The blowing plate body 1 includes a first side, a second side, a third side, a fourth side, a fifth side and a sixth side. The second side and the third side are opposite to the first side, and the fourth side and the fifth side are adjacent to the first side. One end of the fourth side is connected to one end of the first side, and the other end of the fourth side is connected to one end of the second side. One end of the fifth side is connected to the other end of the first side, and the other end of the fifth side is connected to one end of the third side. The other end of the third side is connected to one end of the sixth side, and the other end of the sixth side is connected to the other side of the second side. The first side, the second side, the third side, the fourth side, the fifth side and the sixth side are connected end to end to form an L-shaped structure.
[0023] The length of the first side is 750 mm, the length of the second side is 400 mm, the length of the third side is 350 mm, the length of the fourth side is 450 mm, the length of the fifth side is 150 mm, and the length of the sixth side is 300 mm.
[0024] The partition 3 is made of solid pure aluminum material, which is a circular structure. The radius of the partition 3 is 4.5mm. A number of partitions 3 cover the L-shaped heat transfer area 2 and are arranged in a rectangular array. The part between two adjacent partitions 3 is made into a refrigerant flow channel 4 through a blowing process for the refrigerant to flow. The distance between two adjacent partitions 3 is 4.1-5.2mm. In this embodiment, the distance between two adjacent partitions 3 is 4.5mm. It is proved by calculation and experiment that when the distance between two adjacent partitions 3 is set to 4.5mm, the formed refrigerant flow channel 4 can ensure that the internal pressure reaches 5MPA, which can meet the pressure of most refrigerants and ensure the cooling effect.
[0025] The edge of the heat transfer zone 2 is a wavy structure, which ensures the uniformity of the distance between the edge of the heat transfer zone 2 and the adjacent partition 3, so that the width of the flow channel is always maintained between 4.1 and 5.2 mm, and finally can be maintained at 4.5 mm, thereby ensuring the cooling effect.
[0026] In this application, unless otherwise clearly specified and limited, the terms "connected", "connected", "fixed" and the like should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be an electrical connection; it can be a direct connection, or an indirect connection through an intermediate medium, it can be the internal connection of two elements or the interaction relationship between two elements. For ordinary technicians in this field, the specific meanings of the above terms in this utility model can be understood according to specific circumstances.
[0027] In the specification of the present utility model, a lot of specific details are described. However, it is understood that the embodiments of the present utility model can be practiced without these specific details. In some examples, well-known methods, systems and techniques are not shown in detail so as not to obscure the understanding of this specification.
[0028] In the description of this specification, the description with reference to the terms "one embodiment", "some embodiments", "example", "specific example", or "some examples" etc. means that the specific features, systems, materials or characteristics described in conjunction with the embodiment or example are included in at least one embodiment or example of the utility model. In this specification, the schematic representations of the above terms do not necessarily refer to the same embodiment or example. Moreover, the specific features, systems, materials or characteristics described may be combined in any one or more embodiments or examples in a suitable manner. In addition, those skilled in the art may combine and combine the different embodiments or examples described in this specification and the features of the different embodiments or examples, unless they are contradictory.
[0029] Finally, it should be noted that the above embodiments are only used to illustrate the technical solution of the utility model, rather than to limit it. Although the utility model has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or replace some or all of the technical features therein by equivalents. These modifications or replacements do not make the essence of the corresponding technical solutions deviate from the scope of the technical solutions of the embodiments of the utility model, and they should all be included in the scope of the claims and specification of the utility model.
Claims
1. A blown plate heat exchanger, comprising a blown plate body, wherein the blown plate body has a heat transfer area, characterized in that: A refrigerant filling port is arranged on one side of the heat transfer zone. A plurality of partitions are arranged in the heat transfer zone at intervals. The partitions are circular structures made of pure aluminum. The intervals between the partitions form a refrigerant flow channel.
2. The blown plate heat exchanger according to claim 1, characterized in that: The distance of the refrigerant flow channel is 4.1-5.2 mm.
3. The blown plate heat exchanger according to claim 1, characterized in that: The partitions are arranged in a rectangular array.
4. The blown plate heat exchanger according to claim 1, characterized in that: The edge of the heat transfer zone is a wave-shaped structure.
5. The blown plate heat exchanger according to claim 1, characterized in that: The refrigerant flow channel is manufactured by adopting an inflation process.
6. The inflation plate heat exchanger according to claim 1, characterized in that: The blowing plate body and the heat transfer area are both L-shaped structures.
7. The blown plate heat exchanger according to claim 6, characterized in that: The blowing plate body includes a first side, a second side, a third side, a fourth side and a fifth side, the second side and the third side are opposite to the first side, and the fourth side and the fifth side are adjacent to the first side; the length of the first side is 750mm, the length of the second side is 400mm, the length of the third side is 350mm, the length of the fourth side is 450mm, and the length of the fifth side is 150mm.
Citation Information
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