WO2023284388A1 - Eddy current heat exchange apparatus - Google Patents
Eddy current heat exchange apparatus Download PDFInfo
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- WO2023284388A1 WO2023284388A1 PCT/CN2022/091903 CN2022091903W WO2023284388A1 WO 2023284388 A1 WO2023284388 A1 WO 2023284388A1 CN 2022091903 W CN2022091903 W CN 2022091903W WO 2023284388 A1 WO2023284388 A1 WO 2023284388A1
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- vortex
- channel
- fluid
- heat exchange
- exchange device
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- 239000012530 fluid Substances 0.000 claims abstract description 130
- 239000002131 composite material Substances 0.000 claims abstract description 24
- 238000012546 transfer Methods 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000001816 cooling Methods 0.000 description 7
- 238000013461 design Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000007246 mechanism Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
- F28D7/106—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
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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
- 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
Definitions
- the invention relates to a vortex heat exchange device, in particular to a vortex heat exchange device which performs fluid heat exchange in a vortex manner.
- a heat exchanger is mainly a device that transfers heat through the flow of fluid, thereby achieving the effect of cooling and heating.
- Today's heat exchangers are mainly provided with a heat flow channel and a cooling channel in a detour in a housing.
- the hot flow channel and the cooling channel are mutually interlaced and not communicated with each other, the hot flow channel of the heat exchanger can allow a hot fluid to pass through, and the cooling channel can pass a cold fluid to pass through.
- the hot fluid and the cold fluid can exchange heat through the tube walls of the hot flow channel and the cooling channel during the process of passing through the hot flow channel and the cooling channel respectively, and pass through
- the hot flow channel and cooling channel are designed in a roundabout way to increase the heat transfer area when the hot fluid and the cold fluid pass through, thereby achieving the effect of improving the heat exchange efficiency.
- the technical problem to be solved by the present invention is to provide a vortex heat exchange device, so as to improve the problems of complex structures and high manufacturing and maintenance costs of current heat exchangers.
- the technical solution proposed by the present invention is to provide a vortex heat exchange device, which includes:
- a composite tube assembly which includes an outer tube and an inner tube arranged in the outer tube, a vortex channel extending axially along the inner tube is formed between the outer tube and the inner tube, the outer tube the tube forms a fluid outlet at one end of the vortex channel;
- a vortex guiding structure which is arranged on the composite pipe assembly and is located at the other end of the vortex channel opposite to the fluid outlet, the vortex guiding structure has a fluid inlet connected to the vortex channel, and the fluid inlet
- a high-pressure fluid can be introduced, and the high-pressure fluid can form a vortex after passing through the vortex guide structure and enter the vortex channel, and the high-pressure fluid can exchange heat from the inner tube or the outer tube to the export export.
- the vortex heat exchange device of the present invention can be connected to an external high-pressure fluid supply source at the fluid inlet, wherein the vortex heat exchange device has the following advantages:
- the vortex heat exchange device of the present invention is mainly through the flow path design of the composite tube assembly and the eddy current guiding structure, so that when the high-pressure fluid passes through the vortex guiding structure, the high-pressure fluid can The vortex around the periphery of the inner tube is generated and passes through the vortex channel, which can increase the flow path of the high-pressure fluid in the vortex channel, thereby eliminating the need to design complicated circuitous channels, effectively simplifying the structure, and reducing manufacturing and maintenance costs.
- the vortex heat exchange device of the present invention mainly uses the vortex guide structure to make the high-pressure fluid flow through the vortex channel in a vortex flow, thereby effectively increasing the high-pressure fluid flow.
- the flow path inside the vortex channel can effectively increase the heat transfer area between the high-pressure fluid and the outer tube or inner tube, and can effectively improve the heat exchange efficiency.
- Fig. 1 is the three-dimensional schematic view of the first preferred embodiment of the vortex heat exchange device of the present invention.
- FIG. 2 is a perspective view from another angle of FIG. 1 .
- Fig. 3 is a side view cross-sectional schematic view of the first preferred embodiment of the vortex heat exchange device of the present invention.
- Fig. 4 is a schematic cross-sectional view of A-A in Fig. 3 .
- FIG. 5 is a schematic perspective view of the second preferred embodiment of the vortex heat exchange device of the present invention.
- Fig. 6 It is a side sectional schematic view of the second preferred embodiment of the vortex heat exchange device of the present invention.
- Fig. 7 is a schematic cross-sectional view of B-B in Fig. 6 .
- Fig. 8 It is a three-dimensional schematic view of the third preferred embodiment of the vortex heat exchange device of the present invention.
- FIG. 9 is a schematic perspective view of another angle of FIG. 8 .
- Fig. 10 is a three-dimensional schematic view of the eddy current guide structure, the inner tube and the eddy current guide structure of the third preferred embodiment of the eddy current heat exchange device of the present invention.
- Fig. 11 is a schematic side sectional view of the third preferred embodiment of the vortex heat exchange device of the present invention.
- Fig. 12 is a schematic cross-sectional view of C-C in Fig. 11 .
- Fig. 13 is a perspective schematic diagram of a fourth preferred embodiment of the vortex heat exchange device of the present invention.
- Fig. 14 It is a schematic side sectional view of the fourth preferred embodiment of the vortex heat exchange device of the present invention.
- Fig. 15 is a schematic diagram of the D-D section in Fig. 14 .
- Fig. 16 is a schematic diagram of the application of the eddy current heat exchange device of the present invention in a solar heat collector.
- Figure 17 Schematic diagram of the heat collection method of the solar collector.
- FIG. 18 is a three-dimensional schematic view of various embodiments of the eddy current heat exchange device of the present invention.
- Figure 19 is a schematic diagram of the internal structure of Figure 18.
- FIG. 20 is a schematic side sectional view of FIG. 18 .
- Fig. 21 is a schematic cross-sectional view of E-E in Fig. 20 .
- FIG. 1 , FIG. 5 , FIG. 8 , and FIG. 13 are several preferred embodiments of the vortex heat exchange device of the present invention, which include a composite tube assembly 10a, 10b and a vortex guiding structure 20a, 20b.
- the composite pipe assembly 10a, 10b comprises an outer pipe 11 and an inner pipe 12a, 12b arranged in the outer pipe 11, so A vortex channel 13 extending axially along the inner tubes 12a, 12b is formed between the outer tube 11 and the inner tubes 12a, 12b, and a fluid outlet 14 is formed at one end of the vortex channel 13 by the outer tube 11;
- the opposite ends of the inner tube 12a, 12b can be closed ends; or, as shown in Figure 11 and Figure 14, the outer side of the outer tube 11 can be coated with a partition
- a fluid channel 121 is formed inside the inner tubes 12a, 12b, and the fluid channel 121 has an inlet 122 and an outlet 123, and the inlet 122 of the fluid channel 121 can introduce a working fluid, so The working fluid can exchange heat with the high-pressure fluid after passing through the fluid channel 121 , and
- the eddy current guide structure 20a, 20b is arranged on the composite pipe assembly 10a, 10b, and is located in the vortex channel 13 opposite to the The other end of the fluid outlet 14, the vortex guide structure 20a, 20b has a fluid inlet 21a, 21b connected to the vortex channel 13, the fluid inlet 21a, 21b can introduce a high-pressure fluid, and the high-pressure fluid can pass through The vortex guide structures 20a, 20b then form vortexes and enter the vortex channel 13, and the high-pressure fluid can conduct heat exchange on the inner tubes 12a, 12b or the outer tube 11 and then be exported from the fluid outlet 14.
- the eddy current guiding structure 20a, 20b can have various embodiments, wherein, as shown in Fig. 1, Fig. 4, Fig. 8, and Fig. 10, the vortex guiding structure 20a can have a plurality of helical guiding structures Flow channel 22, the opposite ends of the plurality of guide channels 22 are respectively connected to the vortex channel 13 and the fluid inlet 21a, and the high-pressure fluid can generate vortex when passing through the plurality of guide channels 22; or, As shown in Fig. 7 and Fig. 15, the fluid inlet 21b of the vortex guide structure 20b extends along the tangential direction of the vortex channel 13, so that high-pressure fluid can enter the vortex channel 13 from the fluid inlet 21b in a tangential direction. , so that the high-pressure fluid flows along the tube wall of the outer tube 11 to form a vortex.
- the eddy current heat exchange device can further include at least one eddy current guiding structure 30a, 30b according to requirements, and the vortex guiding structure 30a, 30b are arranged in the vortex channels 13 of the composite pipe assembly 10a, 10b, the vortex guide structures 30a, 30b are spaced apart from the vortex guide structures 20a, 20b, and the vortex guide structures 30a, 30b It includes a plurality of guide channels 31a, 31b arranged in a ring and spiral shape, and the opposite ends of the plurality of guide channels 31a, 31b are formed with an inlet end 311 and an outlet end respectively communicating with the vortex channel 13 312, and the calibers of the plurality of guide channels 31a, 31b are tapered from the inlet end 311 to the outlet end 312, and the high-pressure fluid can be formed when passing through the plurality of guide channels 31a, 31b vortex.
- the vortex heat exchange device includes a deflector 40, the deflector 40 can be arranged in the vortex channel 13 of the composite tube assembly 10a, and the deflector The plate 40 is adjacent to the fluid outlet 14 of the outer tube 11, and a spiral flow channel 41 communicating with the vortex channel 13 is formed in the deflector plate 40, and the spiral flow channel 41 can guide the high-pressure fluid from the Fluid outlet 14 flows out.
- the fluid inlets 21a, 21b of the eddy current guiding structures 20a, 20b of the vortex heat exchange device of the present invention are connected to a high-pressure fluid supply source, and the vortex
- the heat exchange device is mainly designed through the channel design of the composite tube assembly 10a, 10b and the vortex guide structure 20a, 20b, so that when the high-pressure fluid passes through the vortex guide structure 20a, 20b, the high-pressure fluid can generate a surrounding
- the vortex on the periphery of the inner tubes 12a, 12b, and through the vortex channel 13, can increase the flow path of the high-pressure fluid in the vortex channel 13, thus not only does not need to design a complicated circuitous flow channel, but also can effectively simplify the structure and reduce the manufacturing cost. and maintenance costs, in addition, it can effectively increase the heat transfer area between the high-pressure fluid and the outer tube 11 or the inner tube 12b, and can effectively improve the heat exchange
- the eddy current heat exchange device can be configured into various preferred embodiments according to the adjustment of the structure according to the usage requirements, and each embodiment will be described below.
- the opposite ends of the inner tube 12a of the composite tube assembly 10a are closed ends, and the vortex guiding structure 20a can have a plurality of helical guide channels 22, the high-pressure fluid can generate a vortex when passing through the plurality of guide channels 22, and when it passes through the vortex channel 13, it is connected to the outside of the outer tube 11 fluid for heat exchange.
- the opposite ends of the inner tube 12a of the composite tube assembly 10a are closed ends, and the vortex guide
- the fluid inlet 21b of the structure 20b extends along the tangential direction of the vortex channel 13, so that the high-pressure fluid can enter the vortex channel 13 from the fluid inlet 21b in the tangential direction, thereby making the high-pressure fluid flow along the outer tube 11
- the tube wall flows to form a vortex, and exchanges heat with the fluid outside the outer tube 11 when passing through the vortex channel 13 .
- the vortex heat exchange device can include at least one The vortex flow guiding structure 30a, and the outlet ends 312 of the plurality of flow guiding channels 31a of the vortex flow guiding structure 30a are close to the inner side wall of the outer tube 11, so that the high-pressure fluid can pass through the vortex
- the flow guide structure 30a it can flow along the plurality of flow guide channels 31a and flow close to the inner wall of the outer tube 11 , thereby improving the heat transfer efficiency of the high-pressure fluid to the outer tube 11 .
- the inner tube 12b of the composite tube assembly 10b forms the fluid channel 121 inside, and the outer tube 11
- the outer side can be coated or coated with heat insulating material, the working fluid can exchange heat with the high-pressure fluid after passing through the fluid passage 121, and then lead out from the outlet 123, the eddy current guiding structure 20a
- the high-pressure fluid can generate vortex when passing through the multiple guide channels 22, and when passing through the vortex channel 13, it can communicate with the fluid channel of the inner tube 12b
- the working fluid in 121 performs heat exchange.
- the fluid channel 121 is formed inside the inner tube 12b of the composite tube assembly 10b, and the working fluid can pass through
- the fluid inlet 21b of the vortex guiding structure 20b extends along the tangential direction of the vortex channel 13, so that the high-pressure Fluid can enter the vortex channel 13 from the fluid inlet 21b in a tangential direction, thereby causing the high-pressure fluid to flow along the wall of the outer tube 11 to form a vortex, and when passing through the vortex channel 13, it will communicate with the vortex channel 13.
- the working fluid in the fluid passage 121 of the inner tube 12b performs heat exchange.
- the vortex heat exchange device can include at least one The vortex guide structure 30b, the outlet end 312 of the plurality of guide channels 31b of the vortex guide structure 30b is close to the outer wall of the inner tube 12b, so that the high-pressure fluid can pass through the vortex guide When the flow structure 30b is used, it can flow along the plurality of guide channels 31b and flow close to the outer wall of the inner tube 12b, thereby improving the heat transfer efficiency of the high-pressure fluid to the inner tube 12b.
- the eddy current heat exchange device of the present invention has multiple application modes, as shown in Figure 16 and Figure 17, taking the first preferred embodiment of the eddy current heat exchange device of the present invention as an example, the eddy current heat exchange device can be applied in solar collectors Heater 50, wherein, the solar heat collector 50 includes a base 51, a sun tracking drive mechanism 52 and a light collecting cover 53, the sun tracking drive mechanism 52 is arranged on the base 51, and the The light collecting cover 53 is pivotally arranged on the base 51, and is connected and controlled by the sun tracking drive mechanism 52, and the eddy current heat exchange device is arranged on the base 51 of the solar heat collector 50, and is positioned At the pivotal axis between the light collecting cover 53 and the base 51, the solar tracking drive mechanism 52 can drive the light collecting cover 53 to pivot relative to the base 51, so that the light collecting cover 53 can Keep facing the sun as the sun moves, and irradiate the sunlight concentratedly on the outer tube 11 of the vortex heat exchange device.
- the solar tracking drive mechanism 52 can
- the solar heat collector 50 can heat the high-pressure fluid inside the vortex heat exchange device through the radiant heat of sunlight, so that the high-pressure fluid can exchange heat with the outer tube 11 when passing through the vortex passage 13, Furthermore, the high-pressure fluid flows out from the fluid outlet 14 in a state of high temperature and high pressure after heat exchange. Therefore, the vortex heat exchange device can be matched with the solar heat collector 50 and connected with a vortex generator to achieve power generation.
- the eddy current heat exchange device can also be used in conjunction with each other through various preferred embodiments, as shown in Figure 18 to Figure 21, when the first preferred embodiment of the eddy current heat exchange device is matched with the third preferred embodiment
- the user can arrange multiple vortex heat exchange devices of the first preferred embodiment in parallel in the fluid channel 121 of the vortex heat exchange device of the third preferred embodiment, and pass The high-pressure fluid in the vortex heat exchange device of the first preferred embodiment and the high-pressure fluid in the vortex heat exchange device of the third preferred embodiment perform heat exchange on the working fluid in the fluid channel 121 , thereby improving the heat exchange efficiency.
- the vortex heat exchange device is mainly designed through the composite tube assembly 10a, 10b and the flow channel design of the vortex guide structure 20a, 20b, so that the high-pressure fluid passes through the vortex guide structure 20a, 20b can generate a vortex around the periphery of the inner tubes 12a, 12b, thereby increasing the flow path of the high-pressure fluid in the vortex channel 13, not only does not need to design a complicated circuitous flow channel, but also can effectively simplify the structure and reduce manufacturing and maintenance costs ,
- the heat transfer area between the high-pressure fluid and the outer tube 11 or the inner tubes 12a, 12b can be effectively increased, and the heat exchange efficiency can be effectively improved.
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- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
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Abstract
Description
Claims (10)
- 一种涡流热交换装置,其特征在于,其包含:A vortex heat exchange device, characterized in that it comprises:一复合管组件,其包含一外管以及设置在该外管内的一内管,所述外管与所述内管之间形成有沿着该内管轴向延伸的一涡流通道,所述外管在涡流通道的一端形成一流体出口;以及A composite tube assembly, which includes an outer tube and an inner tube arranged in the outer tube, a vortex channel extending axially along the inner tube is formed between the outer tube and the inner tube, the outer tube the tube forms a fluid outlet at one end of the vortex channel; and一涡流导引结构,其是设置在该复合管组件,并位在所述涡流通道相对该流体出口的另一端,所述涡流导引结构具有连通该涡流通道的一流体入口,所述流体入口能导入一高压流体,所述高压流体能在通过该涡流导引结构后形成涡流并进入该涡流通道,所述高压流体能对所述内管或所述外管进行热交换后从所述流体出口导出。A vortex guiding structure, which is arranged on the composite pipe assembly and is located at the other end of the vortex channel opposite to the fluid outlet, the vortex guiding structure has a fluid inlet connected to the vortex channel, and the fluid inlet A high-pressure fluid can be introduced, and the high-pressure fluid can form a vortex after passing through the vortex guide structure and enter the vortex channel, and the high-pressure fluid can exchange heat from the inner tube or the outer tube to the export export.
- 根据权利要求1所述的涡流热交换装置,其特征在于,所述涡流导引结构具有多个螺旋状的导引流道,该多个导引流道的相对二端是分别连通该涡流通道以及该流体入口,所述高压流体能在通过该多个导引流道产生涡流。The vortex heat exchange device according to claim 1, wherein the vortex guiding structure has a plurality of spiral guide channels, and the opposite ends of the plurality of guide channels are respectively connected to the vortex channels As well as the fluid inlet, the high-pressure fluid can generate a vortex when passing through the plurality of guiding channels.
- 根据权利要求1所述的涡流热交换装置,其特征在于,所述涡流导引结构的流体入口是沿着所述涡流通道切线方向延伸。The vortex heat exchange device according to claim 1, wherein the fluid inlet of the vortex guiding structure extends along the tangential direction of the vortex channel.
- 根据权利要求1至3中任一项所述的涡流热交换装置,其特征在于,所述外管外侧能包覆一隔热层,所述内管内部形成一流体通道,所述流体通道具有一导入口及一导出口,所述流体通道的导入口能导入一工作流体,所述工作流体能通过所述流体通道后与所述高压流体进行热交换,并自所述导出口处导出。The vortex heat exchange device according to any one of claims 1 to 3, characterized in that, the outside of the outer tube can be covered with a heat insulating layer, and a fluid channel is formed inside the inner tube, and the fluid channel has An inlet and an outlet. The inlet of the fluid channel can introduce a working fluid, and the working fluid can exchange heat with the high-pressure fluid after passing through the fluid channel, and then be exported from the outlet.
- 根据权利要求1至3中任一项所述的涡流热交换装置,其特征在于,所述涡流热交换装置包含至少一涡流导流结构,所述涡流导流结构是设置在该复合管组件的涡流通道内,所述涡流导流结构与所述涡流导引结构间隔设置,所述涡流导流结构包含环状排列且呈螺旋状的多个导流流道,该多个导流流道的相对二端形成有分别连通该涡流 通道的一入口端及一出口端,且该多个导流流道的口径是自该入口端朝该出口端方向尺寸渐缩,所述高压流体能在通过该多个导流流道时形成涡流。The vortex heat exchange device according to any one of claims 1 to 3, characterized in that, the vortex heat exchange device comprises at least one vortex flow guide structure, and the vortex flow guide structure is arranged on the composite tube assembly In the vortex channel, the vortex guide structure is spaced apart from the vortex guide structure, and the vortex guide structure includes a plurality of circularly arranged and spiral guide channels, and the plurality of guide channels An inlet port and an outlet port respectively connected to the vortex channel are formed at the opposite two ends, and the diameters of the plurality of diversion channels are tapered from the inlet port to the outlet port, and the high-pressure fluid can pass through A vortex is formed when the plurality of diversion channels are formed.
- 根据权利要求4所述的涡流热交换装置,其特征在于,所述涡流热交换装置包含至少一涡流导流结构,所述涡流导流结构是设置在该复合管组件的涡流通道内,所述涡流导流结构与所述涡流导引结构间隔设置,所述涡流导流结构包含环状排列且呈螺旋状的多个导流流道,该多个导流流道的相对二端形成有分别连通该涡流通道的一入口端及一出口端,且该多个导流流道的口径是自该入口端朝该出口端方向尺寸渐缩,所述高压流体能在通过该多个导流流道时形成涡流。The vortex heat exchange device according to claim 4, characterized in that, the vortex heat exchange device comprises at least one vortex flow guide structure, and the vortex flow guide structure is arranged in the vortex channel of the composite tube assembly, said The eddy current guide structure is arranged at intervals with the vortex guide structure, and the vortex guide structure includes a plurality of circularly arranged and spiral guide channels, and the opposite ends of the plurality of guide channels are respectively formed with An inlet end and an outlet end of the vortex channel are connected, and the calibers of the plurality of guide flow channels are tapered from the inlet end to the outlet end, and the high-pressure fluid can pass through the plurality of guide flow channels. A vortex is formed during the passage.
- 根据权利要求5所述的涡流热交换装置,其特征在于,所述涡流导流结构的该多个导流流道的出口端是贴近所述外管的内侧壁。The vortex heat exchange device according to claim 5, characterized in that, the outlet ends of the plurality of guide channels of the vortex guide structure are close to the inner wall of the outer tube.
- 根据权利要求6所述的涡流热交换装置,其特征在于,所述涡流导流结构的该多个导流流道的出口端是贴近所述内管的外侧壁。The vortex heat exchange device according to claim 6, characterized in that, the outlet ends of the plurality of guide channels of the vortex guide structure are close to the outer wall of the inner tube.
- 根据权利要求7所述的涡流热交换装置,其特征在于,所述涡流热交换装置包含一导流板,所述导流板是设置在该复合管组件的涡流通道内,且所述导流板是邻近该外管的流体出口,所述导流板内形成有连通该涡流通道的一螺旋流道,所述螺旋流道能导引所述高压流体自所述流体出口流出。The vortex heat exchange device according to claim 7, characterized in that, the vortex heat exchange device comprises a deflector, and the deflector is arranged in the vortex channel of the composite tube assembly, and the deflector The plate is adjacent to the fluid outlet of the outer tube, and a spiral flow channel communicating with the vortex channel is formed in the guide plate, and the spiral flow channel can guide the high-pressure fluid to flow out from the fluid outlet.
- 根据权利要求8所述的涡流热交换装置,其特征在于,所述涡流热交换装置包含一导流板,所述导流板是设置在该复合管组件的涡流通道内,且所述导流板是邻近该外管的流体出口,所述导流板内形成有连通该涡流通道的一螺旋流道,所述螺旋流道能导引所述高压流体自所述流体出口流出。The vortex heat exchange device according to claim 8, characterized in that, the vortex heat exchange device comprises a deflector, and the deflector is arranged in the vortex channel of the composite tube assembly, and the deflector The plate is adjacent to the fluid outlet of the outer tube, and a spiral flow channel communicating with the vortex channel is formed in the guide plate, and the spiral flow channel can guide the high-pressure fluid to flow out from the fluid outlet.
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AU2022309902A AU2022309902A1 (en) | 2021-07-13 | 2022-05-10 | Eddy current heat exchange apparatus |
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CN202110787604.5 | 2021-07-13 | ||
CN202110787604.5A CN115615217A (en) | 2021-07-13 | 2021-07-13 | Vortex heat exchanger |
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WO2023284388A1 true WO2023284388A1 (en) | 2023-01-19 |
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PCT/CN2022/091903 WO2023284388A1 (en) | 2021-07-13 | 2022-05-10 | Eddy current heat exchange apparatus |
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Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
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GB759440A (en) * | 1953-10-30 | 1956-10-17 | Garrett Corp | Axial flow vortex tube mechanism |
CA606152A (en) * | 1960-10-04 | The Garrett Corporation | Axial flow vortex tube mechanism | |
GB2312276A (en) * | 1996-04-17 | 1997-10-22 | Stephen James Morris | Vortex flow inducer |
US20070143914A1 (en) * | 2003-12-10 | 2007-06-28 | Matsushita Electric Industrial Co., Ltd. | Heat exchanger and washing apparatus comprising the same |
KR20130001544A (en) * | 2011-06-27 | 2013-01-04 | 이방수 | Method of manufacturing the double-wall pipe and double-wall pipe thereof |
CN107764099A (en) * | 2017-10-30 | 2018-03-06 | 清华大学 | Sleeve pipe enhanced heat exchange unit block and penetrate mixing rotational-flow high-efficient double pipe heat exchanger |
CN111707113A (en) * | 2020-06-10 | 2020-09-25 | 东莞理工学院 | Axial blade reverse rotational flow heat exchange sleeve |
CN213748012U (en) * | 2020-08-04 | 2021-07-20 | 太仓陶氏电气有限公司 | High-efficient stable form heat abstractor |
TWI763557B (en) * | 2021-07-13 | 2022-05-01 | 張宏森 | Eddy Current Heat Exchanger |
-
2021
- 2021-07-13 CN CN202110787604.5A patent/CN115615217A/en active Pending
-
2022
- 2022-05-10 WO PCT/CN2022/091903 patent/WO2023284388A1/en active Application Filing
- 2022-05-10 AU AU2022309902A patent/AU2022309902A1/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA606152A (en) * | 1960-10-04 | The Garrett Corporation | Axial flow vortex tube mechanism | |
GB759440A (en) * | 1953-10-30 | 1956-10-17 | Garrett Corp | Axial flow vortex tube mechanism |
GB2312276A (en) * | 1996-04-17 | 1997-10-22 | Stephen James Morris | Vortex flow inducer |
US20070143914A1 (en) * | 2003-12-10 | 2007-06-28 | Matsushita Electric Industrial Co., Ltd. | Heat exchanger and washing apparatus comprising the same |
KR20130001544A (en) * | 2011-06-27 | 2013-01-04 | 이방수 | Method of manufacturing the double-wall pipe and double-wall pipe thereof |
CN107764099A (en) * | 2017-10-30 | 2018-03-06 | 清华大学 | Sleeve pipe enhanced heat exchange unit block and penetrate mixing rotational-flow high-efficient double pipe heat exchanger |
CN111707113A (en) * | 2020-06-10 | 2020-09-25 | 东莞理工学院 | Axial blade reverse rotational flow heat exchange sleeve |
CN213748012U (en) * | 2020-08-04 | 2021-07-20 | 太仓陶氏电气有限公司 | High-efficient stable form heat abstractor |
TWI763557B (en) * | 2021-07-13 | 2022-05-01 | 張宏森 | Eddy Current Heat Exchanger |
Also Published As
Publication number | Publication date |
---|---|
CN115615217A (en) | 2023-01-17 |
AU2022309902A1 (en) | 2023-10-19 |
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