TWI619922B - Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline - Google Patents
Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline Download PDFInfo
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- TWI619922B TWI619922B TW106115210A TW106115210A TWI619922B TW I619922 B TWI619922 B TW I619922B TW 106115210 A TW106115210 A TW 106115210A TW 106115210 A TW106115210 A TW 106115210A TW I619922 B TWI619922 B TW I619922B
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- heat exchange
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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
- F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
- F28D7/0083—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
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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
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/003—Multiple wall conduits, e.g. for leak detection
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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
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
Abstract
本發明藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置,為由呈套合之多層管體所構成,而藉由外層管路之流體包覆於內層管路以對內層管路內之流體作熱交換,以及由外層管路之流體,對接觸於外層管路外圍之固態或流體形態之溫能體作熱傳導,進而構成呈三層環狀之三溫能體熱交換裝置者。 According to the present invention, a three-temperature energy body heat exchange device for external heat transfer through sleeved multilayer pipes and the periphery of the pipeline is composed of sleeved multilayer pipes, and the inner layer pipeline is covered by the fluid of the outer layer pipeline The heat exchange is performed for the fluid in the inner pipeline, and the fluid in the outer pipeline is used to conduct heat transfer to the solid or fluid-shaped thermoelectric body in contact with the periphery of the outer pipeline. People who can heat exchange devices.
Description
本發明藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置,為由呈套合之多層管體所構成,而藉由外層管路之流體包覆於內層管路以對內層管路內之流體作熱交換,以及由外層管路之流體,對接觸於外層管路外圍之固態或流體形態之溫能體作熱傳導,進而構成呈三層環狀之三溫能體熱交換裝置者。 According to the present invention, a three-temperature energy body heat exchange device for external heat transfer through sleeved multilayer pipes and the periphery of the pipeline is composed of sleeved multilayer pipes, and the inner layer pipeline is covered by the fluid of the outer layer pipeline The heat exchange is performed for the fluid in the inner pipeline, and the fluid in the outer pipeline is used to conduct heat transfer to the solid or fluid-shaped thermoelectric body in contact with the periphery of the outer pipeline. People who can heat exchange devices.
傳統由管路外層對外作熱傳導之熱交換裝置,通常為由通過管路之流體與通過管路外層之流體,或與管路外層接觸之固體或流體作均溫,因此只能構成兩溫能體之熱交換裝置。 Traditionally, the heat exchange device that conducts external heat transfer from the outer layer of the pipeline usually uses the fluid passing through the pipeline and the fluid passing through the outer layer of the pipeline, or the solid or fluid in contact with the outer layer of the pipeline to equalize temperature, so it can only constitute two temperature energy. Body heat exchange device.
本發明為一種由管體內外徑較小之內層管路構成第一導流管體(101),第一導流管體(101)為由導熱體所構成,而由第一導流管體(101)之管孔構成第一流路(102),第一流路(102)兩端分別經第一匯流室(103)及第一流體進出口(104),用以供流體形態之第一溫能體(105)進入及流出,以及由管體內徑大於第一流路(102)外徑之外層管路構成第二導流管體(201)構成兩層管體結構,第二導流管體(201)為由導熱體所構成,而由第二導流管體(201)較大之內徑與第一導流管體(101)外徑之管徑差供構成環形斷面之第二流路(202),第二流路(202)兩端分別經第二匯流室(203)及第二流體進出口(204),用以供呈流體形態之第二溫能體(205)進入及流出,其中構成第二流路(202)之外層管路之外圍,為 供接觸於由地層、地表土壤、海洋、河川、湖泊、池塘、流動液流、以及大氣、流動氣流所構成之自然溫能體,或接觸於由人工設置於水槽、水池或容器中之液體所構成之溫能體,溫能體包括呈氣態、液態、或固態溫能體供作為第三溫能體(305),以形成呈三層環狀之三溫能體熱交換功能者,以供由第二溫能體(205)與第一溫能體(105)及與第三溫能體(305)三者之間作溫能熱傳之熱交換者。 The present invention is a first diversion tube body (101) composed of an inner layer pipe with a smaller outer diameter in a tube body. The first diversion tube body (101) is composed of a heat conductor and a first diversion tube. The pipe hole of the body (101) constitutes a first flow path (102), and the two ends of the first flow path (102) pass through the first manifold (103) and the first fluid inlet and outlet (104), respectively, for the first form of the fluid. The temperature energy body (105) enters and exits, and the second diversion body (201) constitutes a two-layer body structure, and the second diversion body is composed of a pipe with an inner diameter larger than the outer diameter of the first flow path (102). The body (201) is composed of a heat conductor, and the difference between the larger inner diameter of the second diversion tube body (201) and the outer diameter of the first diversion tube body (101) is used to form the first section of the annular section. The second flow path (202), the two ends of the second flow path (202) pass through the second combiner chamber (203) and the second fluid inlet and outlet (204), respectively, for the second temperature energy body (205) in the form of a fluid Inflow and outflow, which constitutes the periphery of the outer layer of the second flow path (202), is For contact with natural thermal energy composed of stratum, surface soil, ocean, rivers, lakes, ponds, flowing fluids, and the atmosphere and flowing air, or contact with liquids artificially placed in sinks, ponds or containers The constructed thermal energy body includes a gaseous, liquid, or solid thermal energy body as the third thermal energy body (305), so as to form a three-layer ring-shaped three thermal energy body heat exchange function, for The heat exchanger for temperature energy heat transfer is performed between the second temperature energy body (205), the first temperature energy body (105), and the third temperature energy body (305).
(101)‧‧‧第一導流管體 (101) ‧‧‧First Diversion Tube
(102)‧‧‧第一流路 (102) ‧‧‧First Stream
(103)‧‧‧第一匯流室 (103) ‧‧‧First Confluence Room
(104)‧‧‧第一流體進出口 (104) ‧‧‧First fluid import and export
(105)‧‧‧第一溫能體 (105) ‧‧‧The first thermal energy body
(111)、(222)‧‧‧螺旋導流片 (111), (222) ‧‧‧spiral deflector
(201)‧‧‧第二導流管體 (201) ‧‧‧Second Diversion Tube
(202)‧‧‧第二流路 (202) ‧‧‧Second Stream
(203)‧‧‧第二匯流室 (203) ‧‧‧Second Confluence Room
(204)‧‧‧第二流體進出口 (204) ‧‧‧Second fluid import and export
(205)‧‧‧第二溫能體 (205) ‧‧‧Second Warm Energy
(305)‧‧‧第三溫能體 (305) ‧‧‧ Third Warm Energy
(400)‧‧‧流體泵 (400) ‧‧‧Fluid Pump
(1000)‧‧‧導熱翼片 (1000) ‧‧‧Conductive fins
圖1所示為本發明主要構成結構實施例之前視示意圖。 FIG. 1 is a schematic front view of an embodiment of the main constituent structure of the present invention.
圖2所示為圖1結構實施例之側視剖面示意圖。 FIG. 2 is a schematic side sectional view of the structural embodiment of FIG. 1.
圖3所示為圖1實施例之第三溫能體為流體並設置流體泵動裝置實施例之前視示意圖。 FIG. 3 is a schematic front view of an embodiment in which the third thermal energy body of the embodiment in FIG. 1 is a fluid and a fluid pumping device is provided.
圖4所示為圖3結構實施例之側視剖面示意圖。 FIG. 4 is a schematic side sectional view of the structural embodiment of FIG. 3.
圖5所示為圖1、圖2加設導熱翼片(1000)之實施例前視剖面示意圖。 FIG. 5 is a schematic front cross-sectional view of the embodiment of FIG. 1 and FIG. 2 with a thermally conductive fin (1000).
圖6所示為圖5結構實施例之側視剖面示意圖。 FIG. 6 is a schematic side sectional view of the structural embodiment of FIG. 5.
圖7所示為本發明之第一導流管體(101)外部與第二導流管體(201)內部之間製成具有呈同螺旋流向螺旋導流片(222)之結構,及/或第一導流管體(101)之內部,製成具有呈同螺旋流向螺旋導流片(111)之實施例之前視圖。 FIG. 7 shows a structure in which a spiral guide piece (222) with a spiral flow direction is made between the outside of the first guide tube body (101) and the inside of the second guide tube body (201) of the present invention, and / Or, the front view of the embodiment of the first deflector body (101) is made with a spiral deflector (111) having the same spiral flow direction.
圖8所示為圖7結構實施例之側視剖面示意圖。 FIG. 8 is a schematic side sectional view of the structural embodiment of FIG. 7.
圖9所示為本發明之第一導流管體(101)外部與第二導流管體(201)內部之間製成具有呈不同螺旋流向螺旋導流片(222)之結構,及/或第一導流管體(101)之內部,製成具有呈不同螺旋流向螺旋導流片(111)實施例之前視圖。 FIG. 9 shows a structure in which spiral guide pieces (222) having different spiral flow directions are made between the outside of the first guide tube body (101) and the inside of the second guide tube body (201) of the present invention, and / Or the front view of the embodiment of the first deflector body (101) is made with the spiral deflector (111) with different spiral flow directions.
圖10所示為圖9結構實施例之側視剖面示意圖。 FIG. 10 is a schematic side sectional view of the structural embodiment of FIG. 9.
傳統由管路外層對外作熱傳導之熱交換裝置,通常為由通過管路之流體與通過管路外層之流體,或與管路外層接觸之固體或流體作均溫,因此只能構成兩溫能體之熱交換裝置;本發明藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置,為由呈套合之多層管體所構成,而藉由外層管路之流體包覆於內層管路以對內層管路內之流體作熱交換,以及由外層管路之流體,對接觸於外層管路外圍之固態或流體形態之溫能體作熱傳導,進而構成呈三層環狀之三溫能體熱交換裝置者;本發明為一種由管體內外徑較小之內層管路構成第一導流管體(101),第一導流管體(101)為由導熱體所構成,而由第一導流管體(101)之管孔構成第一流路(102),第一流路(102)兩端分別經第一匯流室(103)及第一流體進出口(104),用以供流體形態之第一溫能體(105)進入及流出,以及由管體內徑大於第一流路(102)外徑之外層管路構成第二導流管體(201)構成兩層管體結構,第二導流管體(201)為由導熱體所構成,而由第二導流管體(201)較大之內徑與第一導流管體(101)外徑之管徑差供構成環形斷面之第二流路(202),第二流路(202)兩端分別經第二匯流室(203)及第二流體進出口(204),用以供呈流體形態之第二溫能體(205)進入及流出,其中構成第二流路(202)之外層管路之外圍,為供接觸於由地層、地表土壤、海洋、河川、湖泊、池塘、流動液流、以及大氣、流動氣流所構成之自然溫能體,或接觸於由人工設置於水槽、水池或容器中之液體所構成之溫能體,溫能體包括呈氣態、液態、或固態溫能體供作為第三溫能體(305),以形成呈三層環狀之三溫能體熱交換功能者,以供由第二溫能體(205)與第一溫能體(105)及與第三溫能體(305)三者之間作溫能熱傳之熱交換者。 Traditionally, the heat exchange device that conducts external heat transfer from the outer layer of the pipeline usually uses the fluid passing through the pipeline and the fluid passing through the outer layer of the pipeline, or the solid or fluid in contact with the outer layer of the pipeline to equalize temperature, so it can only constitute two temperature energy. Body heat exchanging device; the three-temperature energy body heat exchanging device according to the present invention is provided with a sheathed multilayer tube body and a fluid package of an outer layer tube through the sheathed multilayer tube and the periphery of the pipeline. It covers the inner pipeline to exchange heat in the fluid in the inner pipeline, and the fluid in the outer pipeline conducts heat conduction to the solid or fluid temperature energy body in contact with the periphery of the outer pipeline. The present invention is a first diversion tube body (101) composed of an inner layer pipe with a small outer diameter in the tube. The first diversion tube body (101) is The first flow path (102) is formed by the hole of the first diversion tube body (101), and the two ends of the first flow path (102) enter the first flow chamber (103) and the first fluid respectively. The outlet (104) is used for the first temperature energy body (105) in the form of fluid to enter and flow out, and from the tube body The outer layer of the pipe having a diameter larger than the outer diameter of the first flow path (102) constitutes a second deflector body (201) constituting a two-layer body structure. The second deflector body (201) is composed of a heat conductor and The diameter difference between the larger inner diameter of the second diversion tube body (201) and the outer diameter of the first diversion tube body (101) is used to form the second flow path (202) and the second flow path (202) of the annular section. The two ends pass through the second confluence chamber (203) and the second fluid inlet and outlet (204), respectively, for the second temperature energy body (205) in the form of fluid to enter and flow out, which constitutes the second flow path (202). The outer perimeter of the pipeline is for contact with natural thermal energy composed of stratum, surface soil, ocean, rivers, lakes, ponds, flowing fluids, and the atmosphere and flowing air, or contact with artificially installed water tanks, The thermal energy body composed of the liquid in the pool or container. The thermal energy body includes a gaseous, liquid, or solid thermal energy body as the third thermal energy body (305) to form a three-layered three-temperature energy body. The heat exchange function is for the heat exchange between the second temperature energy body (205), the first temperature energy body (105) and the third temperature energy body (305).
茲就其主要構成說明如下: 圖1所示為本發明之主要構成結構實施例之前視示意圖;圖2所示為圖1結構實施例之側視剖面示意圖;如圖1及圖2中所述之藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置,其主要構成為具有一路或一路以上之第一導流管體(101),第一導流管體(101)為由導熱體所構成,而由第一導流管體(101)之管孔構成第一流路(102),第一流路(102)兩端分別經第一匯流室(103)再經第一流體進出口(104)供流體形態之第一溫能體(105)進入及流出,以及在第一導流管體(101)外部套設一路或一路以上管體內徑大於第一導流管體(101)外徑構成第二導流管體(201)構成兩層管體結構,第二導流管體(201)為由導熱體所構成,而由第二導流管體(201)較大之內徑與第一導流管體(101)外徑之管徑差供構成環形斷面之第二流路(202),第二流路(202)兩端分別經第二匯流室(203)再經第二流體進出口(204)供呈流體形態之第二溫能體(205)進入及流出,其中構成第二導流管體(201)之外層為供接觸於液態之流體、或由固態溫能體所構成之第三溫能體(305)進而構成呈三層環狀之三溫能體熱交換裝置者,以供由第二溫能體(205)與第一溫能體(105)及與第三溫能體(305)三者之間作溫能熱傳之熱交換者;上述第一導流管體(101)、第二導流管體(201)可為一路或一路以上所構成者;上述第一導流管體(101)、第二導流管體(201)可為圓型或方型或橢圓型或其他幾何形狀之管體所構成者;上述第一導流管體(101)、第二導流管體(201)可為相同形狀或不同形狀之管體所構成者;上述第一溫能體(105)、第二溫能體(205)可為相同或不同之流體所構成者; 上述第一導流管體(101)中所供流通之第一溫能體(105)及第二導流管體(201)中所供流通之第二溫能體(205)之流向可為相同或相反者。 The main composition is explained as follows: FIG. 1 is a schematic front view of the main structural embodiment of the present invention; FIG. 2 is a schematic side sectional view of the structural embodiment of FIG. 1; and as shown in FIG. 1 and FIG. The three-temperature energy body heat exchange device for external heat transfer on the periphery of the road is mainly composed of one or more first deflectors (101), and the first deflector (101) is composed of a heat conductor. The first flow path (102) is formed by the pipe holes of the first diversion tube body (101), and the two ends of the first flow path (102) are respectively supplied through the first merge chamber (103) and then through the first fluid inlet and outlet (104). The first thermal energy body (105) in the fluid form enters and exits, and one or more pipes are set outside the first diversion pipe body (101) with an inner diameter larger than the outer diameter of the first diversion pipe body (101). The two guide pipe bodies (201) constitute a two-layer pipe structure. The second guide pipe body (201) is composed of a heat conductor, and the second guide pipe body (201) has a larger inner diameter than the first The diameter difference of the outer diameter of the diversion pipe body (101) is used to form the second flow path (202) of the annular section, and the two ends of the second flow path (202) pass through the second manifold (203) and the second fluid respectively. Import and Export (204) The second temperature energy body (205) in the form of a fluid enters and exits, and the outer layer constituting the second guide tube body (201) is a third temperature energy composed of a solid temperature energy body for contact with a fluid in a liquid state. The body (305) further constitutes a three-temperature energy body heat exchange device in a three-layer ring for the second temperature energy body (205), the first temperature energy body (105), and the third temperature energy body (305). ) The heat exchanger for temperature energy heat transfer between the three; the first diversion tube body (101) and the second diversion tube body (201) may be composed of one or more channels; the above-mentioned first diversion body The pipe body (101) and the second diversion pipe body (201) may be round or square or oval or other geometric shapes; the above-mentioned first diversion pipe body (101), the second diversion pipe The flow tube body (201) may be composed of the same shape or different shape of the tube body; the first temperature energy body (105) and the second temperature energy body (205) may be composed of the same or different fluids; The flow direction of the first thermal energy body (105) provided for circulation in the first diversion tube body (101) and the second thermal energy body (205) provided for circulation in the second diversion tube body (201) may be Same or opposite.
此項藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置,於第三溫能體(305)為由氣態或液態流體所構成時,可進一步加設流體泵(400)以泵動第三溫能體(305)增進熱交換效果者;圖3所示為圖1之實施例之第三溫能體為流體並設置流體泵動裝置實施例之前視示意圖;圖4所示為圖3結構實施例之側視剖面示意圖;如圖3及圖4中所示,為進一步加設流體泵(400)以泵動第三溫能體(305)增進熱交換效果者。 This three-temperature energy body heat exchange device for external heat transfer by combining multi-layer pipes and pipelines can be further equipped with a fluid pump (400 when the third temperature energy body (305) is composed of a gaseous or liquid fluid) ) A person who pumps the third temperature energy body (305) to improve the heat exchange effect; FIG. 3 shows a schematic view of the third temperature energy body of the embodiment of FIG. 1 as a fluid and a schematic view of an embodiment of a fluid pumping device; FIG. 4 3 is a schematic side sectional view of the structural embodiment of FIG. 3; as shown in FIG. 3 and FIG. 4, a fluid pump (400) is further added to pump a third temperature energy body (305) to improve the heat exchange effect.
圖5所示為圖1、圖2加設導熱翼片(1000)之實施例前視剖面示意圖;圖6所示為圖5結構實施例之側視剖面示意圖;如圖5及圖6中所示,為於圖1、2實施例中之第二導流管體(201)之間進一步設置導熱翼片(1000),供第二導流管體(201)與第三溫能體(305)間作溫能傳導者。 FIG. 5 is a schematic front sectional view of the embodiment in which thermally conductive fins (1000) are added in FIG. 1 and FIG. 2; FIG. 6 is a schematic side sectional view of the structural embodiment of FIG. 5; It is shown that a thermally conductive fin (1000) is further provided between the second diversion tube body (201) in the embodiment of FIGS. 1 and 2 for the second diversion tube body (201) and the third thermal energy body (305). ) Intercropped with thermal energy.
此項藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置,進一步為將第一導流管體(101)外部與第二導流管體(201)內部之間製成具有螺旋導流片(222)之結構,及/或第一導流管體(101)之內部,製成具有螺旋導流片(111)之結構以增加熱傳效果者,茲說明如下:圖7所示為本發明之第一導流管體(101)外部與第二導流管體(201)內部之間製成具有呈同螺旋流向螺旋導流片(222)之結構,及/或第一導流管體(101)之內部,製成具有呈同螺旋流向螺旋導流片(111)之實施例之前視圖; 圖8所示為圖7結構實施例之側視剖面示意圖;如圖7及圖8中所示,其中供構成此項藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置之第一導流管體(101)外部與第二導流管體(201)內部之間製成具有呈同螺旋流向螺旋導流片(222)之結構,及/或第一導流管體(101)之內部,製成具有呈同螺旋流向螺旋導流片(111)之結構。 This three-temperature energy body heat exchange device for external heat transfer by fitting a multilayer pipe and the outer periphery of the pipeline further makes the system between the outside of the first diversion tube body (101) and the inside of the second diversion tube body (201). Those who have formed a structure with a spiral deflector (222) and / or the inside of the first guide tube body (101) and made a structure with a spiral deflector (111) to increase the heat transfer effect are described below: FIG. 7 shows a structure in which a spiral guide piece (222) with a spiral flow direction is made between the outside of the first guide tube body (101) and the inside of the second guide tube body (201) of the present invention, and / Or the front view of the embodiment of the first guide pipe body (101), which is made with the spiral guide plate (111) having the same spiral flow direction; Fig. 8 is a schematic side sectional view of the structural embodiment of Fig. 7; as shown in Figs. 7 and 8, the three-temperature energy heat exchange for external heat transfer constituting this borrowed and nested multilayer pipe and pipeline is shown in Figs. The device has a structure having a spiral flow deflector (222) with the same spiral flow direction between the outside of the first flow guide body (101) and the inside of the second flow guide body (201), and / or the first flow guide The inside of the body (101) is made to have a structure having a spiral flow guide (111) having the same spiral flow direction.
圖9所示為本發明之第一導流管體(101)外部與第二導流管體(201)內部之間製成具有呈不同螺旋流向螺旋導流片(222)之結構,及/或第一導流管體(101)之內部,製成具有呈不同螺旋流向螺旋導流片(111)實施例之前視圖;圖10所示為圖9結構實施例之側視剖面示意圖;如圖9及圖10中所示,其中供構成此項藉套合多層管及管路外圍對外熱傳之三溫能體熱交換裝置之第一導流管體(101)外部與第二導流管體(201)內部之間製成具有呈不同螺旋流向螺旋導流片(222)之結構,及/或第一導流管體(101)之內部,製成具有呈不同螺旋流向螺旋導流片(111)之結構。 FIG. 9 shows a structure in which spiral guide pieces (222) having different spiral flow directions are made between the outside of the first guide tube body (101) and the inside of the second guide tube body (201) of the present invention, and / Or the inside of the first diversion tube body (101), a front view of the embodiment of the spiral deflector (111) with different spiral flow directions; FIG. 10 is a schematic side sectional view of the structural embodiment of FIG. 9; As shown in Fig. 9 and Fig. 10, the outer part of the first diversion tube body (101) and the second diversion tube for the three-temperature energy heat exchange device for external heat transfer of the multi-layer tube and the periphery of the pipeline are provided. The structure of the spiral guides (222) with different spiral flow directions is made between the interior of the body (201), and / or the spiral guides with different spiral flow directions is made inside the first guide tube body (101). (111) structure.
Claims (12)
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US13/628,116 | 2012-09-27 | ||
US13/628,116 US20140083666A1 (en) | 2012-09-27 | 2012-09-27 | Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline and Transferring Heat to Exterior Through Outer Periphery of Pipeline |
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TW201730495A TW201730495A (en) | 2017-09-01 |
TWI619922B true TWI619922B (en) | 2018-04-01 |
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TW106115210A TWI619922B (en) | 2012-09-27 | 2013-09-27 | Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline |
TW102134914A TWI586932B (en) | 2012-09-27 | 2013-09-27 | Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline |
TW102218081U TWM476252U (en) | 2012-09-27 | 2013-09-27 | Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline |
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TW102134914A TWI586932B (en) | 2012-09-27 | 2013-09-27 | Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline |
TW102218081U TWM476252U (en) | 2012-09-27 | 2013-09-27 | Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline |
Country Status (8)
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US (1) | US20140083666A1 (en) |
EP (1) | EP2713131B1 (en) |
JP (2) | JP6401439B2 (en) |
CN (3) | CN203501858U (en) |
AU (2) | AU2013234402B2 (en) |
CA (1) | CA2828311C (en) |
SG (1) | SG2013073028A (en) |
TW (3) | TWI619922B (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140083666A1 (en) * | 2012-09-27 | 2014-03-27 | Tai-Her Yang | Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline and Transferring Heat to Exterior Through Outer Periphery of Pipeline |
CN105972869B (en) * | 2016-06-14 | 2019-02-12 | 杨胜东 | A kind of big channel evaporative condenser dual-purpose heat exchanger and its system |
CN106197088A (en) * | 2016-08-19 | 2016-12-07 | 张家港市德胜染整有限责任公司 | A kind of waste-heat recovery device of dyeing waste-water |
EP3808444A4 (en) | 2018-06-12 | 2022-02-23 | IHI Corporation | Reaction device |
CN109210967B (en) * | 2018-09-17 | 2020-01-14 | 中国核动力研究设计院 | Multi-stage sleeve heat exchanger for reactor fuel testing loop |
CZ308768B6 (en) * | 2020-03-17 | 2021-05-05 | Vysoká Škola Báňská - Technická Univerzita Ostrava | Recuperative screw heat exchanger, especially for bulk materials |
CN113464216B (en) * | 2021-07-28 | 2023-07-28 | 湖南湘化机汽轮机有限公司 | Steam turbine for waste heat recovery of steam boiler |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW495013U (en) * | 2001-12-04 | 2002-07-11 | Taiwan Reduce Pollutant Techno | Heat exchanger |
WO2009062487A2 (en) * | 2007-11-14 | 2009-05-22 | GEA Luftkühler GmbH | Heat exchanger |
Family Cites Families (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1798330A (en) * | 1925-09-18 | 1931-03-31 | Leek Albert Edward | Heat-exchange apparatus |
US1738914A (en) * | 1926-08-04 | 1929-12-10 | George T Mott | Apparatus for heat exchanging |
US1701341A (en) * | 1928-02-24 | 1929-02-05 | Frick Co | Cooling coil |
US2658728A (en) * | 1948-06-25 | 1953-11-10 | Lummus Co | Method of detecting leakage between heat transfer fluids |
US2858677A (en) * | 1955-04-11 | 1958-11-04 | Marley Co | Water cooling apparatus |
JPS5756071Y2 (en) * | 1977-04-16 | 1982-12-03 | ||
US4210199A (en) * | 1978-06-14 | 1980-07-01 | Doucette Industries, Inc. | Heat exchange system |
JPS58136985A (en) * | 1982-02-08 | 1983-08-15 | Mitsubishi Electric Corp | Heat exchanger |
FR2552216B1 (en) * | 1983-09-21 | 1988-08-12 | Onera (Off Nat Aerospatiale) | IMPROVEMENTS TO HEAT EXCHANGER TUBES AND TO EXCHANGERS MADE WITH SUCH TUBES |
DE3411675A1 (en) * | 1984-03-27 | 1985-10-10 | Josef Hubert 5203 Much Schick | DEVICE FOR EXCHANGING HEAT AND FUEL BETWEEN TWO OR MORE FLOWABLE MEDIA |
JPS6159188A (en) * | 1984-08-30 | 1986-03-26 | Toyo Radiator Kk | Charge air cooler |
JPS63154967U (en) * | 1987-03-30 | 1988-10-12 | ||
JPH03279789A (en) * | 1990-03-28 | 1991-12-10 | Yanmar Diesel Engine Co Ltd | Double piped heat exchanger |
CN2094021U (en) * | 1991-05-25 | 1992-01-22 | 程效民 | Tube in tube tubular heat-exchanger |
JPH09113168A (en) * | 1995-10-13 | 1997-05-02 | Tokyo Gas Co Ltd | Double tube type vaporizer |
JP2001280864A (en) * | 2000-03-30 | 2001-10-10 | Hitachi Ltd | Heat exchanger and manufacturing method therefor |
CN2449174Y (en) * | 2000-10-25 | 2001-09-19 | 于奎明 | Large volume sleeve pipe type heat-exchanger |
JP2003050092A (en) * | 2001-08-06 | 2003-02-21 | Ee R C:Kk | Heat exchanger |
CN2588308Y (en) * | 2002-11-26 | 2003-11-26 | 郝德欣 | Cold and hot water exchanger for central heating |
JP2005127684A (en) * | 2003-10-27 | 2005-05-19 | Atago Seisakusho:Kk | Double tube type heat exchanger |
JP4033402B2 (en) * | 2004-04-27 | 2008-01-16 | 本田技研工業株式会社 | Heat exchanger |
CN1719179A (en) * | 2005-07-11 | 2006-01-11 | 刘庆久 | Pipe heat exchanger |
CN200947001Y (en) * | 2006-04-30 | 2007-09-12 | 华南理工大学 | Sleeve-type heat exchanger |
WO2008078194A2 (en) * | 2006-06-20 | 2008-07-03 | Adir Segal, Ltd. | Thermal load management system |
CN101105373A (en) * | 2007-08-01 | 2008-01-16 | 中原工学院 | Fin-sleeve type three mediums composite heat-exchanger |
JP2009162395A (en) * | 2007-12-28 | 2009-07-23 | Showa Denko Kk | Double-wall-tube heat exchanger |
CN101226033A (en) * | 2008-02-18 | 2008-07-23 | 中原工学院 | Shell-sleeve type three-medium composite heat exchanger |
CN201407930Y (en) * | 2009-06-01 | 2010-02-17 | 刘洪亮 | Highly-effective sewage heat exchanger |
CN102042774A (en) * | 2009-10-16 | 2011-05-04 | 杨泰和 | Heat absorption or release device with flow paths distributed alternatively and evenly according to temperature difference |
JP5743051B2 (en) * | 2010-09-15 | 2015-07-01 | 三浦工業株式会社 | Heat exchanger and boiler water supply system |
CN201945215U (en) * | 2010-12-27 | 2011-08-24 | 青岛磐石容器制造有限公司 | Fixed tube plate type double-tube heat exchanger |
US20140083666A1 (en) * | 2012-09-27 | 2014-03-27 | Tai-Her Yang | Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline and Transferring Heat to Exterior Through Outer Periphery of Pipeline |
-
2012
- 2012-09-27 US US13/628,116 patent/US20140083666A1/en not_active Abandoned
-
2013
- 2013-09-26 CA CA2828311A patent/CA2828311C/en active Active
- 2013-09-27 SG SG2013073028A patent/SG2013073028A/en unknown
- 2013-09-27 TW TW106115210A patent/TWI619922B/en active
- 2013-09-27 CN CN201320600892.XU patent/CN203501858U/en not_active Expired - Lifetime
- 2013-09-27 TW TW102134914A patent/TWI586932B/en active
- 2013-09-27 TW TW102218081U patent/TWM476252U/en not_active IP Right Cessation
- 2013-09-27 EP EP13186548.7A patent/EP2713131B1/en active Active
- 2013-09-27 AU AU2013234402A patent/AU2013234402B2/en active Active
- 2013-09-27 CN CN201910500868.0A patent/CN110274494A/en active Pending
- 2013-09-27 CN CN201310448066.2A patent/CN103697725A/en active Pending
- 2013-09-27 JP JP2013200948A patent/JP6401439B2/en active Active
-
2017
- 2017-11-28 AU AU2017268511A patent/AU2017268511A1/en not_active Abandoned
-
2018
- 2018-09-06 JP JP2018166800A patent/JP6746647B2/en active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW495013U (en) * | 2001-12-04 | 2002-07-11 | Taiwan Reduce Pollutant Techno | Heat exchanger |
WO2009062487A2 (en) * | 2007-11-14 | 2009-05-22 | GEA Luftkühler GmbH | Heat exchanger |
Also Published As
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TW201730495A (en) | 2017-09-01 |
AU2013234402A1 (en) | 2014-04-10 |
CN103697725A (en) | 2014-04-02 |
JP6746647B2 (en) | 2020-08-26 |
TWM476252U (en) | 2014-04-11 |
AU2017268511A1 (en) | 2017-12-14 |
JP6401439B2 (en) | 2018-10-10 |
JP2014074581A (en) | 2014-04-24 |
US20140083666A1 (en) | 2014-03-27 |
CN203501858U (en) | 2014-03-26 |
CA2828311C (en) | 2020-07-28 |
CN110274494A (en) | 2019-09-24 |
JP2019007729A (en) | 2019-01-17 |
TWI586932B (en) | 2017-06-11 |
AU2013234402A2 (en) | 2017-03-02 |
EP2713131A1 (en) | 2014-04-02 |
TW201416638A (en) | 2014-05-01 |
CA2828311A1 (en) | 2014-03-27 |
EP2713131B1 (en) | 2016-06-08 |
AU2013234402B2 (en) | 2017-09-21 |
SG2013073028A (en) | 2014-04-28 |
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