WO2023284388A1 - Eddy current heat exchange apparatus - Google Patents

Eddy current heat exchange apparatus Download PDF

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Publication number
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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WO
WIPO (PCT)
Prior art keywords
vortex
channel
fluid
heat exchange
exchange device
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PCT/CN2022/091903
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French (fr)
Chinese (zh)
Inventor
张宏森
张宇婕
Original Assignee
张宏森
张宇婕
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Application filed by 张宏森, 张宇婕 filed Critical 张宏森
Priority to AU2022309902A priority Critical patent/AU2022309902A1/en
Publication of WO2023284388A1 publication Critical patent/WO2023284388A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-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
    • F28D7/106Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements 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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  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
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Abstract

The present invention relates to an eddy current heat exchange apparatus, which comprises a composite pipe component and an eddy current guide structure provided in the composite pipe component; the composite pipe component comprises an outer pipe and an inner pipe provided in the outer pipe, wherein an eddy current channel extending along the axial direction of the inner pipe is formed between the outer pipe and the inner pipe, a fluid outlet is formed in the outer pipe at the end of the eddy current channel, the eddy current guide structure is located at the other end of the eddy current channel relative to the fluid outlet, and a fluid inlet that communicates with the eddy current channel is provided; a high-pressure fluid can be introduced from the fluid inlet, and the high-pressure fluid can generate eddy currents surrounding the periphery of the inner pipe when passing through the eddy current guide structure, thereby increasing flow paths of the high-pressure fluid in the eddy current channel. Thus, not only can the structure be effectively simplified, fabrication and maintenance costs can be reduced, but the heat transfer area between the high-pressure fluid and the outer pipe or the inner pipe can also be effectively increased, and heat exchange efficiency can be effectively improved.

Description

涡流热交换装置Vortex Heat Exchanger 技术领域technical field
本发明是一种涡流热交换装置,尤指利用涡流的方式进行流体热交换的涡流热交换装置。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.
背景技术Background technique
热交换器主要是通过流体的流动以进行热量的传递的装置,由此达到冷却以及升温的效果,现今的热交换器主要是通过在一壳体内迂回设置有一热流通道以及一冷却通道,所述热流通道与所述冷却通道是相互交错且互不连通,所述热交换器的热流通道能供一热流体通过,而所述冷却通道能通一冷流体通过。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.
当在进行热交换时,所述热流体及所述冷流体能分别在通过所述热流通道及所述冷却通道的过程中,通过所述热流通道、冷却通道的管壁进行热交换,并通过迂回设计的热流通道及冷却通道,以提高热流体与冷流体通过时的热传面积,进而达到提高热交换效率的效果。When performing heat exchange, 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.
然而现今的热交换器必须设计复杂的迂回流道以提高热传导的效率,不但结构复杂,且在制造及维护的成本较高,故仍有待改善的必要。However, today's heat exchangers must be designed with complex circuitous channels to improve the efficiency of heat conduction. Not only is the structure complex, but also the cost of manufacturing and maintenance is high, so there is still a need for improvement.
发明内容Contents of the invention
本发明所要解决的技术问题是:提供一种涡流热交换装置,以借此改善现今的热交换器结构复杂,且在制造及维护的成本较高的问题。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.
本发明所提出的技术解决方案是:提供一种涡流热交换装置,其包含:The technical solution proposed by the present invention is to provide a vortex heat exchange device, which includes:
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.
本发明涡流热交换装置能通过在所述流体入口处连接外部的高压流体供应源,其中,所述涡流热交换装置具备有下列优点: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:
1.简化结构并降低成本:本发明涡流热交换装置主要是通过所述复合管组件及涡流导引结构的流道设计,使所述高压流体在通过所述涡流导引结构时,高压流体能产生环绕内管外围的涡流,并通过所述涡流通道,能增加所述高压流体在涡流通道内的流动路径,由此无需设计复杂的迂回流道,能有效简化结构,降低制造及维护成本。1. Simplify the structure and reduce the cost: 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.
2.提高热交换效率:如前述,本发明涡流热交换装置主要是通过所述涡流导引结构使所述高压流体以涡流流动的方式通过所述涡流通道,由此能有效增加所述高压流体在所述涡流通道内部的流动路径,由此能有效增加所述高压流体与外管或是内管之间的热传面积,能有效提高热交换效率。2. Improve heat exchange efficiency: As mentioned above, 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.
附图说明Description of drawings
图1:为本发明涡流热交换装置的第一种较佳实施例的立体示意图。Fig. 1: is the three-dimensional schematic view of the first preferred embodiment of the vortex heat exchange device of the present invention.
图2:为图1的另一角度的立体示意图。FIG. 2 : is a perspective view from another angle of FIG. 1 .
图3:为本发明涡流热交换装置的第一种较佳实施例的侧视剖面示意图。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.
图4:为图3的A-A剖面示意图。Fig. 4: is a schematic cross-sectional view of A-A in Fig. 3 .
图5:为本发明涡流热交换装置的第二种较佳实施例的立体示意图。FIG. 5 : is a schematic perspective view of the second preferred embodiment of the vortex heat exchange device of the present invention.
图6:为本发明涡流热交换装置的第二种较佳实施例的侧视剖面示意图。Fig. 6: It is a side sectional schematic view of the second preferred embodiment of the vortex heat exchange device of the present invention.
图7:为图6的B-B剖面示意图。Fig. 7: is a schematic cross-sectional view of B-B in Fig. 6 .
图8:为本发明涡流热交换装置的第三种较佳实施例的立体示意图。Fig. 8: It is a three-dimensional schematic view of the third preferred embodiment of the vortex heat exchange device of the present invention.
图9:为图8的另一角度的立体示意图。FIG. 9 : is a schematic perspective view of another angle of FIG. 8 .
图10:为本发明涡流热交换装置的第三种较佳实施例的涡流导引结构、内管及涡流导流结构的立体示意图。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.
图11:为本发明涡流热交换装置的第三种较佳实施例的侧视剖面示意图。Fig. 11: is a schematic side sectional view of the third preferred embodiment of the vortex heat exchange device of the present invention.
图12:为图11的C-C剖面示意图。Fig. 12: is a schematic cross-sectional view of C-C in Fig. 11 .
图13:为本发明涡流热交换装置的第四种较佳实施例的立体示意图。Fig. 13 is a perspective schematic diagram of a fourth preferred embodiment of the vortex heat exchange device of the present invention.
图14:为本发明涡流热交换装置的第四种较佳实施例的侧视剖面示意图。Fig. 14: It is a schematic side sectional view of the fourth preferred embodiment of the vortex heat exchange device of the present invention.
图15:为图14的D-D剖面示意图。Fig. 15 is a schematic diagram of the D-D section in Fig. 14 .
图16:为本发明涡流热交换装置应用在太阳能集热器的示意图。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.
图17:为太阳能集热器的集热方式示意图。Figure 17: Schematic diagram of the heat collection method of the solar collector.
图18:为本发明涡流热交换装置的多种实施例搭配应用的立体示意图。FIG. 18 : is a three-dimensional schematic view of various embodiments of the eddy current heat exchange device of the present invention.
图19:为图18的内部结构示意图。Figure 19: is a schematic diagram of the internal structure of Figure 18.
图20:为图18的侧视剖面示意图。FIG. 20 : is a schematic side sectional view of FIG. 18 .
图21:为图20的E-E剖面示意图。Fig. 21: is a schematic cross-sectional view of E-E in Fig. 20 .
附图标记说明:Explanation of reference signs:
10a,10b:复合管组件         11:外管10a, 10b: Composite pipe assembly 11: Outer pipe
12a,12b:内管               121:流体通道12a, 12b: inner tube 121: fluid channel
122:导入口                 123:导出口122: import port 123: export port
13:涡流通道                14:流体出口13: Vortex channel 14: Fluid outlet
15:隔热层                  20a,20b:涡流导引结构15: Heat insulation layer 20a, 20b: Vortex guide structure
21a,21b:流体入口           22:导引流道21a, 21b: Fluid inlet 22: Guide channel
30a,30b:涡流导流结构       31a,31b:导流流道30a, 30b: vortex diversion structure 31a, 31b: diversion channel
311:入口端                 312:出口端311: Entry port             312: Exit port
40:导流板                  41:螺旋流道40: deflector 41: spiral flow channel
50:太阳能集热器            51:基座50: Solar collector 51: Base
52:追日驱动机构            53:集光罩52: Sun-tracking drive mechanism 53: Photocollector cover
具体实施方式detailed description
以下配合附图及本发明的较佳实施例,进一步阐述本发明为达成预定发明目的所采取的技术手段。In the following, the technical means adopted by the present invention to achieve the intended purpose of the invention will be further described in conjunction with the accompanying drawings and preferred embodiments of the present invention.
请参阅图1、图5、图8、图13,为本发明涡流热交换装置的数种较佳实施例,其包含一复合管组件10a,10b及一涡流导引结构20a,20b。Please refer to FIG. 1 , FIG. 5 , FIG. 8 , and FIG. 13 , which 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.
如图1、图2、图5、图8、图9、图13所示,该复合管组件10a,10b包含一外管11以及设置在该外管11内的一内管12a,12b,所述外管11与所述内管12a,12b之间形成有沿着该内管12a,12b轴向延伸的一涡流通道13,所述外管11在涡流通道13的一端形成一流体出口14;其中,如图3、图6所示,所述内管12a,12b的相对二端可以为封闭端;或是,如图11、图14所示,所述外管11外侧能包覆一隔热层15,所述内管12a,12b内部形成一流体通道121,所述流体通道121具有一导入口122及一导出口123,所述流体通道121的导入口122能导入一工作流体,所述工作流体能通过所述流体通道121后与所述高压流体进行热交换,并自所述导出口123处导出。As shown in Fig. 1, Fig. 2, Fig. 5, Fig. 8, Fig. 9, and Fig. 13, 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; Wherein, as shown in Figure 3 and Figure 6, 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 In the thermal layer 15, 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 is exported from the outlet 123 .
如图1、图4、图7、图8、图10、图15所示,该涡流导引结构20a,20b是设置在该复合管组件10a,10b,并位在所述涡流通道13相对该流体出口14的另一端,所述涡流导引结构20a,20b具有连通该涡流通道13的一流体入口21a,21b,所述流体入口21a,21b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20a,20b后形成涡流并进入该涡流通道13,所述高压流体能对所述内管12a,12b或所述外管11进行热交换后从所述流体出口14导出。As shown in Fig. 1, Fig. 4, Fig. 7, Fig. 8, Fig. 10, and Fig. 15, 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.
所述涡流导引结构20a,20b可以有多种的实施方式,其中,如图1、图4、图8、图10所示,所述涡流导引结构20a能具有多个螺旋状的导引流道22,该多个导引流道22的相对二端是分别连通该涡流通道13以及该流体入口21a,所述高压流体能在通过该多个导引流道22产生涡流;或是,如图7、图15所示,所述涡流导引结构20b的流体入口21b是沿着所述涡流通道13切线方向延伸,使高压流体能自所述流体入口21b以切线方向进入涡流通道13内,由此使高压流体的沿着所述外管11的管壁流动而形成涡流。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.
此外,如图2、图3、图6、图10、图11、图14所示,所述涡流热交换装置能依据需求进一步包含至少一涡流导流结构30a,30b,所述 涡流导流结构30a,30b是设置在该复合管组件10a,10b的涡流通道13内,所述涡流导流结构30a,30b与所述涡流导引结构20a,20b间隔设置,所述涡流导流结构30a,30b包含环状排列且呈螺旋状的多个导流流道31a,31b,该多个导流流道31a,31b的相对二端形成有分别连通该涡流通道13的一入口端311及一出口端312,且该多个导流流道31a,31b的口径是自该入口端311朝该出口端312方向尺寸渐缩,所述高压流体能在通过该多个导流流道31a,31b时形成涡流。In addition, as shown in Fig. 2, Fig. 3, Fig. 6, Fig. 10, Fig. 11, and Fig. 14, 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.
再者,如图2、图3所示,所述涡流热交换装置包含一导流板40,所述导流板40能设置在该复合管组件10a的涡流通道13内,且所述导流板40是邻近该外管11的流体出口14,所述导流板40内形成有连通该涡流通道13的一螺旋流道41,所述螺旋流道41能导引所述高压流体自所述流体出口14流出。Furthermore, as shown in Fig. 2 and Fig. 3, 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.
如图2、图3、图6、图10、图11、图14所示,本发明涡流热交换装置的涡流导引结构20a,20b的流体入口21a,21b连接高压流体供应源,所述涡流热交换装置主要是通过所述复合管组件10a,10b及涡流导引结构20a,20b的流道设计,使所述高压流体在通过所述涡流导引结构20a,20b时,高压流体能产生环绕内管12a,12b外围的涡流,并通过所述涡流通道13,能增加所述高压流体在涡流通道13内的流动路径,由此不但无需设计复杂的迂回流道,能有效简化结构,降低制造及维护成本,此外,能有效增加所述高压流体与外管11或是内管12b之间的热传面积,能有效提高热交换效率。As shown in Fig. 2, Fig. 3, Fig. 6, Fig. 10, Fig. 11, and Fig. 14, 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 efficiency.
其中,所述涡流热交换装置能依据使用需求调整结构而设定成多种较佳实施例,以下分别针对各实施例进行说明。Wherein, 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.
如图1至图4所示,在本发明涡流热交换装置的第一种较佳实施例中,所述复合管组件10a的内管12a的相对二端为封闭端,所述涡流导引结构20a能具有多个螺旋状的所述导引流道22,所述高压流体能在通过该多个导引流道22产生涡流,并在通过所述涡流通道13时与所述外管11外侧的流体进行热交换。As shown in Figures 1 to 4, in the first preferred embodiment of the vortex heat exchange device of the present invention, 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.
如图5至图7所示,另在本发明涡流热交换装置的第二种较佳实施例中,所述复合管组件10a的内管12a的相对二端为封闭端,所述涡流导引结构20b的流体入口21b是沿着所述涡流通道13切线方向延 伸,使高压流体能自所述流体入口21b以切线方向进入涡流通道13内,由此使高压流体的沿着所述外管11的管壁流动而形成涡流,并在通过所述涡流通道13时与所述外管11外侧的流体进行热交换。As shown in Figures 5 to 7, in the second preferred embodiment of the vortex heat exchange device of the present invention, 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 .
其中,如图2、图3、图6所示,在本发明涡流热交换装置的第一种较佳实施例与第二种较佳实施例中,所述涡流热交换装置能包含至少一所述涡流导流结构30a,且所述涡流导流结构30a的该多个导流流道31a的出口端312是贴近所述外管11的内侧壁,由此能使高压流体在通过所述涡流导流结构30a时,能顺着该多个导流流道31a流动并贴近所述外管11的内侧壁流动,进而提高所述高压流体对所述外管11的热传效率。Wherein, as shown in Fig. 2, Fig. 3 and Fig. 6, in the first preferred embodiment and the second preferred embodiment of the vortex heat exchange device of the present invention, 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 When the flow guide structure 30a is used, 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 .
如图8至图12所示,在本发明涡流热交换装置的第三种较佳实施例中,所述复合管组件10b的内管12b内部形成所述流体通道121,且所述外管11的外侧能包覆或涂布隔热材料,所述工作流体能通过所述流体通道121后与所述高压流体进行热交换,并自所述导出口123处导出,所述涡流导引结构20a具有多个螺旋状的所述导引流道22,所述高压流体能在通过该多个导引流道22产生涡流,并在通过所述涡流通道13时与所述内管12b的流体通道121内的工作流体进行热交换。As shown in Figures 8 to 12, in the third preferred embodiment of the vortex heat exchange device of the present invention, 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 There are multiple spiral guide channels 22, 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.
如图13至图15所示,在本发明涡流热交换装置的第四种较佳实施例中,所述复合管组件10b的内管12b内部形成所述流体通道121,所述工作流体能通过所述流体通道121后与所述高压流体进行热交换,并自所述导出口123处导出,所述涡流导引结构20b的流体入口21b是沿着所述涡流通道13切线方向延伸,使高压流体能自所述流体入口21b以切线方向进入涡流通道13内,由此使高压流体的沿着所述外管11的管壁流动而形成涡流,并在通过所述涡流通道13时与所述内管12b的流体通道121内的工作流体进行热交换。As shown in Figures 13 to 15, in the fourth preferred embodiment of the vortex heat exchange device of the present invention, the fluid channel 121 is formed inside the inner tube 12b of the composite tube assembly 10b, and the working fluid can pass through After the fluid channel 121 performs heat exchange with the high-pressure fluid, and leads out from the outlet 123, 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.
其中,如图8、图10、图15所示,在本发明涡流热交换装置的第三种较佳实施例与第四种较佳实施例中,所述涡流热交换装置能包含至少一所述涡流导流结构30b,所述涡流导流结构30b的该多个导流流道31b的出口端312是贴近所述内管12b的外侧壁,由此能使高压流体在通过所述涡流导流结构30b时,能顺着该多个导流流道31b流动并贴近所述内管12b的外侧壁流动,进而提高所述高压流体对所述内 管12b的热传效率。Wherein, as shown in Fig. 8, Fig. 10 and Fig. 15, in the third preferred embodiment and the fourth preferred embodiment of the vortex heat exchange device of the present invention, 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.
本发明涡流热交换装置具有多种应用方式,如图16、图17所示,以本发明涡流热交换装置的第一种较佳实施例为例,所述涡流热交换装置能应用在太阳能集热器50,其中,所述太阳能集热器50包含一基座51、一追日驱动机构52以及一集光罩53,所述追日驱动机构52是设置在该基座51上,且所述集光罩53是枢设在该基座51上,并连接受控在该追日驱动机构52,所述涡流热交换装置是设置在该太阳能集热器50的基座51上,并位在所述集光罩53与所述基座51的枢接轴心处,所述追日驱动机构52能带动该集光罩53相对该基座51枢转,使所述集光罩53能随着太阳的移动而保持面向太阳,并将阳光集中照射在所述涡流热交换装置的外管11。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.
其中,所述太阳能集热器50能通过太阳光的辐射热加热所述涡流热交换装置内部的高压流体,使所述高压流体在通过所述涡流通道13时与所述外管11热交换,进而让所述高压流体在热交换后呈现高温高压的状态自所述流体出口14流出,因此,所述涡流热交换装置能搭配太阳能集热器50并连接一涡流发电机以达到发电的效果。Wherein, 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.
此外,所述涡流热交换装置亦能通过多种较佳实施例之间相互搭配应用,如图18至图21所示,当所述涡流热交换装置的第一种较佳实施例搭配第三种较佳实施例时,使用者能在一个所述第三种较佳实施例的涡流热交换装置的流体通道121内部并联设置多个第一种较佳实施例的涡流热交换装置,并通过该多个第一种较佳实施例的涡流热交换装置内部的高压流体以及所述第三种较佳实施例的涡流热交换装置的高压流体对所述流体通道121内部的工作流体进行热交换,由此提高热交换效率。In addition, 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 In a 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.
综上所述,所述涡流热交换装置主要是通过所述复合管组件10a,10b及涡流导引结构20a,20b的流道设计,使所述高压流体在通过所述涡流导引结构20a,20b时能产生环绕内管12a,12b外围的涡流,由此能增加所述高压流体在涡流通道13内的流动路径,不但无需设计复杂的迂回流道,能有效简化结构,降低制造及维护成本,此外,能有效增加所述高压流体与外管11或是内管12a,12b之间的热传面积,能有效提高热交换效率。In summary, 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 , In addition, 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.
以上所述仅是本发明的较佳实施例而已,并非对本发明做任何形式上的限制,虽然本发明已以较佳实施例揭示如上,然而并非用以限定本发明,任何本领域技术人员,在不脱离本发明技术方案的范围内,当可利用上述揭示的技术内容作出些许更动或修饰为等同变化的等效实施例,但凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。The above description is only a preferred embodiment of the present invention, and does not limit the present invention in any form. Although the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Any person skilled in the art, Within the scope of not departing from the technical solution of the present invention, when the technical content disclosed above can be used to make some changes or be modified into equivalent embodiments with equivalent changes, but all the content that does not depart from the technical solution of the present invention, according to the technical content of the present invention In essence, any simple modifications, equivalent changes and modifications made to the above embodiments still fall within the scope of the technical solution of the present invention.

Claims (10)

  1. 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.
  2. 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.
  3. 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.
  4. 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.
  5. 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.
  6. 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.
  7. 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.
  8. 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.
  9. 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.
  10. 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.
PCT/CN2022/091903 2021-07-13 2022-05-10 Eddy current heat exchange apparatus WO2023284388A1 (en)

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CN202110787604.5A CN115615217A (en) 2021-07-13 2021-07-13 Vortex heat exchanger

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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Patent Citations (9)

* Cited by examiner, † Cited by third party
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

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