TW201416638A - 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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- TW201416638A TW201416638A TW102134914A TW102134914A TW201416638A TW 201416638 A TW201416638 A TW 201416638A TW 102134914 A TW102134914 A TW 102134914A TW 102134914 A TW102134914 A TW 102134914A TW 201416638 A TW201416638 A TW 201416638A
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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
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
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。 The three-temperature energy heat exchange device of the present invention is composed of a multi-layer heat pipe exchanging the outer layer of the multi-layer pipe and the outer heat of the pipeline, and is composed of a multi-layered pipe body which is sleeved, and the fluid of the outer layer pipe is coated on the inner layer pipeline The heat exchange between the fluid in the inner pipeline and the fluid in the outer pipeline is used to conduct heat conduction to the solid or fluid form of the warm energy body contacting the outer periphery of the outer conduit, thereby forming a three-layered three-temperature The body heat exchange device.
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。 Conventionally, the heat exchange device for external heat conduction from the outer layer of the pipeline is usually made of a fluid passing through the pipeline and a fluid passing through the outer layer of the pipeline or a solid or fluid in contact with the outer layer of the pipeline, so that only two temperatures can be formed. 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 invention is a first guiding tube body (101) composed of an inner layer pipe having a small outer diameter inside the tube body, the first guiding tube body (101) is composed of a heat conducting body, and the first guiding tube is composed of a first guiding tube The tube hole of the body (101) constitutes a first flow path (102), and the two ends of the first flow path (102) respectively pass through the first confluence chamber (103) and the first fluid inlet and outlet (104) for the first form of the fluid The warm energy body (105) enters and flows out, and the inner diameter of the pipe body is larger than the outer diameter of the first flow path (102), and the second flow guiding pipe body (201) constitutes a two-layer pipe structure, and the second draft tube The body (201) is composed of a heat conductor, and the difference between the inner diameter of the larger diameter of the second draft tube body (201) and the outer diameter of the first draft tube body (101) is the first to form a circular section. The second flow path (202) and the second flow path (202) are respectively a second confluence chamber (203) and a second fluid inlet and outlet (204) for entering and flowing out of the second warm energy body (205) in a fluid form, wherein the outer flow path of the second flow path (202) is formed Peripheral, for access to natural warm bodies consisting of strata, surface soils, oceans, rivers, lakes, ponds, flowing streams, and atmospheric, flowing air streams, or in contact with artificially installed sinks, sinks or containers The warm energy body composed of the liquid, the warm energy body includes a gaseous, liquid, or solid temperature body as the third warm energy body (305) to form a three-layered three-temperature heat exchange function. For heat exchange between the second warm energy body (205) and the first warm energy body (105) and the third warm energy body (305) for heat transfer.
(101)‧‧‧第一導流管體 (101)‧‧‧First diversion tube body
(102)‧‧‧第一流路 (102)‧‧‧First flow path
(103)‧‧‧第一匯流室 (103)‧‧‧First confluence chamber
(104)‧‧‧第一流體進出口 (104)‧‧‧First fluid import and export
(105)‧‧‧第一溫能體 (105)‧‧‧First warm energy body
(111)、(222)‧‧‧螺旋導流片 (111), (222)‧‧‧Spiral baffles
(201)‧‧‧第二導流管體 (201)‧‧‧Second diversion tube body
(202)‧‧‧第二流路 (202)‧‧‧Second flow path
(203)‧‧‧第二匯流室 (203) ‧‧‧Second junction 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 body
(305)‧‧‧第三溫能體 (305) ‧‧‧ third warm energy body
(400)‧‧‧流體泵 (400)‧‧‧ fluid pump
(1000)‧‧‧導熱翼片 (1000)‧‧‧thermal 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 front elevational view showing an embodiment of a main constitution of the present invention.
圖2所示為圖1結構實施例之側視剖面示意圖。 2 is a side cross-sectional view showing 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。 3 is a front elevational view showing an embodiment in which the third warm energy body of the embodiment of FIG. 1 is 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。 4 is a side cross-sectional view showing 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 front cross-sectional view showing an embodiment in which the heat conducting fins (1000) are added to FIGS. 1 and 2.
圖6所示為圖5結構實施例之側視剖面示意圖。 Figure 6 is a side cross-sectional view showing the structural embodiment of Figure 5.
圖7所示為圖1、圖2中各段第一導流管體(101)呈串聯,包覆於第一導流管體(101)外部之各段第二導流管體(201)亦呈串聯之實施例前視示意圖。 Figure 7 shows the first draft tube body (101) of each segment in Figure 1 and Figure 2 in series, and the second draft tube body (201) wrapped around the outside of the first draft tube body (101). A front view of an embodiment in series is also shown.
圖8所示為圖7結構實施例之側視剖面示意圖。 Figure 8 is a side elevational cross-sectional view of the structural embodiment of Figure 7.
圖9所示為圖5、圖6中各段第一導流管體(101)呈串聯,包覆於第一導流管體(101)外部之各段第二導流管體(201)亦呈串聯之實施例前視示意圖。 Figure 9 is a view showing the first draft tube body (101) of each stage in Fig. 5 and Fig. 6 in series, and the second draft tube body (201) wrapped around the outside of the first draft tube body (101). A front view of an embodiment in series is also shown.
圖10所示為圖9結構實施例之側視剖面示意圖。 Figure 10 is a side cross-sectional view showing the structural embodiment of Figure 9.
圖11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。 Figure 11 shows the inside of the first draft tube body (101) of the present invention and the inside of the second draft tube body (201). An embodiment having a spiral spiral flow guide piece (222) in the same spiral direction and/or a first flow guiding pipe body (101) is formed to have a spiral flow guiding piece (111) in the same spiral flow direction. Previous view.
圖12所示為圖11結構實施例之側視剖面示意圖。 Figure 12 is a side cross-sectional view showing the structural embodiment of Figure 11.
圖13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。 Figure 13 shows a structure in which the outer portion of the first draft tube body (101) and the second draft tube body (201) are formed with different spiral flow directions to the spiral baffle (222), and / Or the inside of the first draft tube body (101) is made to have a front view with an embodiment of a different spiral flow direction to the spiral baffle (111).
圖14所示為圖13結構實施例之側視剖面示意圖。 Figure 14 is a side cross-sectional view showing the structural embodiment of Figure 13;
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。 Conventionally, the heat exchange device for external heat conduction from the outer layer of the pipeline is usually made of a fluid passing through the pipeline and a fluid passing through the outer layer of the pipeline or a solid or fluid in contact with the outer layer of the pipeline, so that only two temperatures can be formed. The heat exchange device of the body; the three-temperature energy heat exchange device for external heat transfer of the multi-layer pipe and the outer periphery of the pipeline is composed of a multi-layered tubular body, and the fluid package of the outer pipeline Covering the inner layer pipeline to exchange heat with the fluid in the inner layer pipeline, and the fluid of the outer layer pipeline is used for heat conduction to the solid body or fluid form of the warm energy body contacting the outer layer pipeline, thereby forming three The invention relates to a three-temperature heat exchanger heat exchange device; the invention comprises a first flow guiding pipe body (101) formed by an inner layer pipe having a small outer diameter inside the pipe body, and the first guiding pipe body (101) is The first flow path (102) is formed by the tube hole of the first flow guiding tube body (101), and the first flow path (102) is respectively fed through the first collecting chamber (103) and the first fluid into the first flow path (102). An outlet (104) for entering and flowing out of the first warm energy body (105) in the form of a fluid, and in the tube body The diameter of the outer tube is larger than the outer diameter of the first flow path (102), and the second flow guiding tube body (201) constitutes a two-layer tubular body structure, and the second guiding tube body (201) is composed of a heat conducting body, and The difference between the larger inner diameter of the second draft tube body (201) and the outer diameter of the outer diameter of the first draft tube body (101) is to form a second flow path (202) of the annular cross section, and the second flow path (202) The two ends are respectively passed through the second confluence chamber (203) and the second fluid inlet and outlet (204) for supplying the fluid The second warm energy body (205) of the form enters and flows out, and constitutes the outer periphery of the outer flow path of the second flow path (202) for contacting the ground layer, the surface soil, the ocean, the river, the lake, the pond, the flowing liquid a warm body composed of a stream, a natural warm body composed of an atmosphere or a flowing air stream, or a liquid body composed of a liquid manually placed in a water tank, a pool or a container, the warm energy body including a gaseous state, a liquid state, or a solid state temperature energy. The body is provided as a third warm energy body (305) to form a three-layered three-temperature heat exchange function for the second warm energy body (205) and the first warm energy body (105) and A heat exchanger for heat transfer between the third and the second warm 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)之外層為供接觸於氣態或液態之流體、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,包括由氣態或液態或氣態轉液態或液態轉氣態之流體所構成者;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。 BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a front view of a main structural embodiment of the present invention; FIG. 2 is a side cross-sectional view of the structural embodiment of FIG. 1; FIG. 1 and FIG. The three-temperature energy heat exchange device of the multi-layer pipe and the outer heat transfer of the pipeline is mainly composed of a first draft pipe body (101) having one or more roads, and a first air guiding pipe body (101) ) is composed of a heat conductor, and the first flow path (102) is formed by the tube hole of the first flow guiding tube body (101), and the first flow path (102) is respectively passed through the first collecting chamber (103) and then a fluid inlet and outlet (104) for entering and flowing out of the first warm energy body (105) in the form of a fluid, and arranging one or more tubes outside the first draft tube body (101) with an inner diameter larger than the first draft tube The outer diameter of the body (101) constitutes a second flow guiding tube body (201) to form a two-layer tubular body structure, the second guiding tube body (201) is composed of a heat conducting body, and the second guiding tube body (201) The difference between the larger inner diameter and the outer diameter of the outer diameter of the first draft tube body (101) is to form a second flow path (202) of the annular section, and the second flow, the two ends of the road (202) respectively pass through the second confluence room (203) passing through the second fluid inlet and outlet (204) for the second warm energy body (205) in the form of a fluid to enter and exit, wherein the outer layer of the second draft tube body (201) is configured to be in contact with the gaseous or liquid state. The fluid or the third warm energy body (305) composed of the solid temperature warm body further constitutes a three-layered three-temperature heat exchanger heat exchange device for the second warm energy body (205) and the first a heat exchanger for heat transfer between a warm energy body (105) and a third warm energy body (305); The first guiding tube body (101) and the second guiding tube body (201) may be formed by one way or more; the first guiding tube body (101) and the second guiding tube body (201) It may be a circular or square or elliptical or other geometric tube; the first guiding tube body (101) and the second guiding tube body (201) may be tubes of the same shape or different shapes. The first warm energy body (105) and the second warm energy body (205) may be composed of the same or different fluids, including a fluid which is changed from a gaseous state or a liquid state or a gaseous state to a liquid state or a liquid gas state. The flow direction of the first warm energy body (105) and the second warm energy body (205) to be circulated in the first flow guiding tube body (101) Can be the same or the 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。 The three-temperature energy heat exchange device for the external heat transfer of the multi-layer pipe and the outer periphery of the pipeline can be further provided with a fluid pump when the third warm energy body (305) is composed of a gaseous or liquid fluid. The pumping of the third warm energy body (305) to enhance the heat exchange effect; FIG. 3 is a front view of the embodiment of the third warm energy body of the embodiment of FIG. 1 being fluid and providing a fluid pumping device; FIG. A side cross-sectional view of the structural embodiment of FIG. 3 is shown; as shown in FIGS. 3 and 4, a fluid pump (400) is further added to pump the third warm energy body (305) to enhance 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。 5 is a front cross-sectional view showing an embodiment of the heat conducting fin (1000) of FIG. 1 and FIG. 2; and FIG. 6 is a side cross-sectional view showing the structural embodiment of FIG. 5; FIG. 5 and FIG. Further, a heat conducting fin (1000) is further disposed between the second draft tube body (201) in the embodiment of FIGS. 1 and 2, and the second guiding tube body (201) and the third warming body (305) are provided. ) Intermittent temperature energy transmission.
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,其第一導流管體(101)及第二導流管體(201)除如圖1、2所示由各管段呈並聯外,進一步將第一導流管體(101)及第二導流管體(201)呈串聯結構者;茲說明如下:圖7所示為圖1、圖2中各段第一導流管體(101)呈串聯,包覆於第一導流管體(101)外部之各段第二導流管體(201)亦呈串聯之實施例前視示意圖;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,為將圖1、2實施例中之第一導流管體(101)呈串聯,第二導流管體(201)之各管段製成串聯聯結者,第一導流管體(101)為由導熱體所構成,第一流路(102)經第一匯流室(103)與至少一第一導流管體(101)之第一流路(102)串聯,再由串聯後之第一流路(102)兩端分別通往第一流體進出口(104),用以供流體形態之第一溫能體(105)進入及流出,以及在第一導流管體(101)外部套設管體內徑大於第一導流管體(101)外徑之第二導流管體(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)經第二匯流室(203)與至少一第二導流管體(201)之第二流路(202)串聯,再由串聯後之第二流路(202)兩端分別通往第二流體進出口(204),用以供呈流體形態之第二溫能體(205)進入及流出,其中構成第二導流管體(201)之外層為供接觸於氣態或液態之流體、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。 In addition to the three-temperature energy heat exchange device of the multi-layer pipe and the outer heat transfer of the pipeline, the first air guiding body (101) and the second air guiding body (201) are not shown in FIG. It is shown that each pipe section is connected in parallel, and the first draft pipe body (101) and the second air guiding pipe body (201) are further connected in series; the following is explained: FIG. 7 shows each of FIG. 1 and FIG. The first guiding tube body (101) is connected in series, and the second guiding tube body (201) covering each section of the first guiding tube body (101) is also in a front view of the embodiment; FIG. 7 is a side cross-sectional view of the structural embodiment of FIG. 7; as shown in FIG. 7 and FIG. 8, the first diversion tube body (101) in the embodiment of FIGS. Each pipe segment of the pipe body (201) is made in series, the first air guiding pipe body (101) is composed of a heat conductor, and the first flow path (102) passes through the first collecting chamber (103) and at least a first guide. The first flow path (102) of the flow tube body (101) is connected in series, and then the two ends of the first flow path (102) connected to the first fluid inlet and outlet (104) are respectively connected to the first temperature energy of the fluid form. Body (105) enters and exits, and in the first draft tube body (101) The second guiding tube body (201) having an inner diameter larger than the outer diameter of the first guiding tube body (101) constitutes a two-layer tube structure, and the second guiding tube body (201) is composed of a heat conductor The second inner flow path (202) of the annular cross section is formed by the larger inner diameter of the second draft tube body (201) and the outer diameter of the outer diameter of the first draft tube body (101). The flow path (202) is connected in series with the second flow path (202) of the at least one second flow guiding tube body (201) via the second collecting chamber (203), and then the two ends of the second flow path (202) after being connected in series And a second fluid inlet and outlet (204) for entering and flowing out of the second warm energy body (205) in a fluid form, wherein the outer layer of the second draft tube body (201) is configured to be in contact with the gaseous or liquid state The fluid or the third warm energy body (305) composed of the solid temperature warm body further constitutes a three-layered three-temperature heat exchanger heat exchange device for the second warm energy body (205) and the first A heat exchanger for heat transfer between a warm energy body (105) and a third warm energy body (305).
圖9所示為圖5、圖6中各段第一導流管體(101)呈串聯,包覆於第一導流管體(101)外部之各段第二導流管體(201)亦呈串聯之 實施例前視示意圖;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,為將圖5、6實施例中之第一導流管體(101)及包覆於第一導流管體(101)外部之第二導流管體(201)之各管段製成串聯聯結者。 Figure 9 is a view showing the first draft tube body (101) of each stage in Fig. 5 and Fig. 6 in series, and the second draft tube body (201) wrapped around the outside of the first draft tube body (101). Also in tandem FIG. 10 is a side cross-sectional view showing the structural embodiment of FIG. 9; as shown in FIG. 9 and FIG. 10, the first guiding tube body in the embodiment of FIGS. 5 and 6 (101) And the tube segments of the second draft tube body (201) coated on the outside of the first draft tube body (101) are made in series.
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11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12所示為圖11結構實施例之側視剖面示意圖;如圖11及圖12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。 The three-temperature energy heat exchange device for external heat transfer of the multi-layer pipe and the outer periphery of the pipeline is further configured to make the outer portion of the first flow guiding pipe body (101) and the second air guiding pipe body (201) The structure having the spiral baffle (222) and/or the inside of the first draft tube (101) is made with a structure having a spiral baffle (111) to increase the heat transfer effect, as explained below: Figure 11 shows a structure in which the outer portion of the first draft tube body (101) of the present invention and the interior of the second draft tube body (201) are formed to have the same spiral flow direction to the spiral baffle (222), and / Or the inside of the first draft tube body (101), the front view of the embodiment having the same spiral flow direction to the spiral baffle (111); FIG. 12 is a side cross-sectional view of the structure embodiment of FIG. As shown in FIG. 11 and FIG. 12, the outer and second diversion of the first diversion tube body (101) for the three-temperature energy heat exchange device constituting the external heat transfer of the multi-layer tube and the outer periphery of the pipeline The inside of the pipe body (201) is formed with a spiral flow guiding piece (222) flowing in the same spiral direction, and/or the inside of the first guiding pipe body (101), and is formed into a spiral flow. A helical baffle (111) of the structure.
圖13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14所示為圖13結構實施例之側視剖面示意圖;如圖13及圖14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。 Figure 13 shows a structure in which the outer portion of the first draft tube body (101) and the second draft tube body (201) are formed with different spiral flow directions to the spiral baffle (222), and / Or the inside of the first draft tube body (101) is formed with a front view of the spiral flow deflector (111) embodiment with different spiral flow directions; FIG. 14 is a side cross-sectional view of the structural embodiment of FIG. 13; 13 and shown in Figure 14, in which the multi-layer tube is constructed And a spiral flow deflector having a different spiral flow direction between the outer portion of the first draft tube body (101) and the second guide tube body (201) of the three-temperature energy heat exchange device of the external heat transfer of the pipeline The structure of (222), and/or the inside of the first draft tube body (101), is formed to have a spiral flow direction to the spiral baffle (111).
(101)‧‧‧第一導流管體 (101)‧‧‧First diversion tube body
(102)‧‧‧第一流路 (102)‧‧‧First flow path
(103)‧‧‧第一匯流室 (103)‧‧‧First confluence chamber
(104)‧‧‧第一流體進出口 (104)‧‧‧First fluid import and export
(105)‧‧‧第一溫能體 (105)‧‧‧First warm energy body
(201)‧‧‧第二導流管體 (201)‧‧‧Second diversion tube body
(202)‧‧‧第二流路 (202)‧‧‧Second flow path
(203)‧‧‧第二匯流室 (203) ‧‧‧Second junction 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 body
(305)‧‧‧第三溫能體 (305) ‧‧‧ third warm energy body
Claims (14)
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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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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) |
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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 |
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-
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
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2017
- 2017-11-28 AU AU2017268511A patent/AU2017268511A1/en not_active Abandoned
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2018
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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 |
TWI619922B (en) | 2018-04-01 |
JP2019007729A (en) | 2019-01-17 |
TWI586932B (en) | 2017-06-11 |
AU2013234402A2 (en) | 2017-03-02 |
EP2713131A1 (en) | 2014-04-02 |
CA2828311A1 (en) | 2014-03-27 |
EP2713131B1 (en) | 2016-06-08 |
AU2013234402B2 (en) | 2017-09-21 |
SG2013073028A (en) | 2014-04-28 |
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