CN103697725A - 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
- Publication number
- CN103697725A CN103697725A CN201310448066.2A CN201310448066A CN103697725A CN 103697725 A CN103697725 A CN 103697725A CN 201310448066 A CN201310448066 A CN 201310448066A CN 103697725 A CN103697725 A CN 103697725A
- Authority
- CN
- China
- Prior art keywords
- diversion tube
- heat
- wen nengti
- fluid
- pipeline
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- 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
-
- 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
-
- 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
-
- 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
Landscapes
- 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
The present invention provides a tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline, which is configured by multiple layers of pipelines sleeved with each other, the fluid in the outer layer pipeline covers the inner layer pipeline for exchanging heat with the fluid in the inner layer pipeline, and the fluid in the outer layer pipeline is further used for transferring heat to the solid or fluid state thermal energy body which is in contact with the outer periphery of the outer layer pipeline, thereby forming a three-layer annular tri-piece thermal energy body heat exchanger.
Description
Technical field
The present invention's invention relates to a kind of fit multilayer pipe and pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing, being specifically related to a kind of multilayer body by being fit is formed, fluid by outer pipeline is coated on internal layer pipeline so that the fluid in internal layer pipeline is done to heat exchange, and by the fluid of outer pipeline, to being contacted with the Wen Nengti work heat conduction of the solid-state or flow morphology of outer pipeline periphery, and then form the three temperature energy body heat switches that are shellring shape.
Background technology
Tradition is externally made heat conducting heat-exchange device by pipeline skin, is generally by the fluid by pipeline and by the outer field fluid of pipeline, or makes samming with the outer solid or liquid contacting of pipeline, therefore can only form the heat-exchange device of two Wen Nengti.
Summary of the invention
The object of the present invention is to provide a kind of fit multilayer pipe and pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing, it forms by being the multilayer body of fit, fluid by outer pipeline is coated on internal layer pipeline so that the fluid in internal layer pipeline is done to heat exchange, and by the fluid of outer pipeline, to being contacted with the Wen Nengti of the solid-state or flow morphology of outer pipeline periphery, do hot conduction, and then form three warm can body heat exchanges that are shellring shape.
In order to achieve the above object, the invention provides a kind of fit multilayer pipe and pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing, its main composition is the first diversion tube having more than a Huo Yi road, road, the first diversion tube consists of heat carrier, and form the first stream by the pore of the first diversion tube, the first Wen Nengti that the first stream two ends are imported and exported for flow morphology through first fluid through first chamber of confluxing respectively again enters and flows out, and at the outside sheathed above internal diameter of tube body in Huo Yi road, road of the first diversion tube, be greater than the first diversion tube external diameter and form the second diversion tube and form two-layer pipe structure, the second diversion tube consists of heat carrier, and by poor the second stream for looping section of the caliber of the larger internal diameter of the second diversion tube and the first diversion tube external diameter, the second stream two ends are imported and exported for the second Wen Nengti that is flow morphology and are entered and flow out through second fluid again through second chamber of confluxing respectively, the skin that wherein forms the second diversion tube is the fluid for being contacted with gaseous state or liquid state, or the 3rd Wen Nengti being formed by solid-state Wen Nengti and then form be three temperature of shellring shape can body heat switches, for by the second Wen Nengti and the first Wen Nengti and and the 3rd Wen Nengti three between do the heat exchange that Wen Nengre passes.
Further comprise the first diversion tube, by heat carrier, formed, the first stream is connected with the first stream of at least one the first diversion tube through first chamber of confluxing, by the first stream two ends after series connection, leading to respectively first fluid again imports and exports, use the first Wen Nengti for flow morphology enter and flow out, and the second diversion tube that is greater than the first diversion tube external diameter at the outside sheathed internal diameter of tube body of the first diversion tube forms two-layer pipe structure, the second diversion tube consists of heat carrier, and by poor the second stream for looping section of the caliber of the larger internal diameter of the second diversion tube and the first diversion tube external diameter, the second stream is connected with the second stream of at least one the second diversion tube through second chamber of confluxing, by the second stream two ends after series connection, leading to respectively second fluid again imports and exports, use for the second Wen Nengti that is flow morphology and enter and flow out, the skin that wherein forms the second diversion tube is the fluid for being contacted with gaseous state or liquid state, or the 3rd Wen Nengti being formed by solid-state Wen Nengti and then form be three temperature of shellring shape can body heat switches, for by the second Wen Nengti and the first Wen Nengti and and the 3rd Wen Nengti three between do the heat exchange that Wen Nengre passes.
Described the first diversion tube, the second diversion tube can be bodys round or square or ellipse or other geometries and form.
Described the first diversion tube, the second diversion tube are formed by identical shaped or difform body.
Described the first Wen Nengti, the second Wen Nengti are formed by identical or different fluid.
Described fluid comprises by gas or liquid or gaseous state turns liquid state or the liquid fluid that turns gaseous state is formed.
Described the 3rd Wen Nengti is containing being consisted of fluid or solid.
Described the 3rd Wen Nengti when consisting of fluid, can further add fluid pump and promote heat exchange effect with moving the 3rd Wen Nengti of pump.
It is identical or contrary in described the first diversion tube, supplying institute in the first Wen Nengti of circulation and the second diversion tube to supply the flow direction of the second Wen Nengti of circulating.
Described fit multilayer pipe comprises by two-layer or two-layer above heat carrier and forming, and form relative number object diversion tube, for supplying by identical or different fluid in each body, its direction of flow that is fit adjacent tubes interlayer different fluid pipeline is identical or contrary.
Between described the second diversion tube, heat conduction fin is further set.
Further for will first diversion tube outside with the second diversion tube inside between make the structure with spiral flow deflector, and/or the inside of the first diversion tube, make there is spiral flow deflector structure to increase heat biography effect.
Between outside and the second diversion tube inside of described the first diversion tube, make to have and be same spiral flow to the structure of spiral flow deflector, and/or the inside of the first diversion tube, make to have and be same spiral flow to the structure of spiral flow deflector.
Described the first diversion tube outside from the second diversion tube inside between make to have and be different spiral flows to the structure of spiral flow deflector, and/or the inside of the first diversion tube, makes to have and is different spiral flows to the structure of spiral flow deflector.
Adopt after such scheme, the present invention is by forming the first diversion tube by the less internal layer pipeline of body internal-and external diameter, the first diversion tube is by being consisted of heat carrier, and form the first stream by the pore of the first diversion tube, the first stream two ends are imported and exported through the first conflux chamber and first fluid respectively, use the first Wen Nengti for flow morphology enter and flow out, and by the outer pipeline that internal diameter of tube body is greater than the first stream external diameter, form the second diversion tube and form two-layer pipe structure, the second diversion tube is consisted of heat carrier, and by poor the second stream for looping section of the caliber of the larger internal diameter of the second diversion tube and the first diversion tube external diameter, the second stream two ends are imported and exported through the second conflux chamber and second fluid respectively, use for the second Wen Nengti that is flow morphology and enter and flow out, wherein form the periphery of the outer pipeline of the second stream, for supplying to be contacted with by stratum, surface soil, ocean, rivers and creeks, lake, pond, flow stream, and atmosphere, the natural Wen Nengti that air flow forms, or be contacted with by being manually arranged at tank, the Wen Nengti that liquid in pond or container forms, Wen Nengti comprises and is gaseous state, liquid, or solid-state Wen Nengti is provided as the 3rd Wen Nengti, to form the three temperature energy body heat functions of exchange that are shellring shape, for by the second Wen Nengti and the first Wen Nengti and and the 3rd Wen Nengti three between do the heat exchange that Wen Nengre passes.
Accompanying drawing explanation
Figure 1 shows that the front-view schematic diagram of main composition structure embodiment of the present invention;
Figure 2 shows that the side-looking generalized section of Fig. 1 structure embodiment;
The 3rd Wen Nengti that Figure 3 shows that Fig. 1 embodiment is fluid the front-view schematic diagram that the moving device embodiment of fluid pump is set;
Figure 4 shows that the side-looking generalized section of Fig. 3 structure embodiment;
Figure 5 shows that Fig. 1, Fig. 2 add the embodiment forward sight generalized section of heat conduction fin;
Figure 6 shows that the side-looking generalized section of Fig. 5 structure embodiment;
Figure 7 shows that in Fig. 1, Fig. 2, each section the first diversion tube is series connection, each section the second diversion tube that is coated on the first diversion tube outside is also the embodiment front-view schematic diagram of series connection;
Figure 8 shows that the side-looking generalized section of Fig. 7 structure embodiment;
Figure 9 shows that in Fig. 5, Fig. 6, each section the first diversion tube is series connection, each section the second diversion tube that is coated on the first diversion tube outside is also the embodiment front-view schematic diagram of series connection;
Figure 10 shows that the side-looking generalized section of Fig. 9 structure embodiment;
Figure 11 shows that to make to have between outside and the second diversion tube inside of the first diversion tube of the present invention and be same spiral flow to the structure of spiral flow deflector, and/or the inside of the first diversion tube, make to have and be same spiral flow to the front view of the embodiment of spiral flow deflector;
Figure 12 shows that the side-looking generalized section of Figure 11 structure embodiment;
Figure 13 shows that the first diversion tube of the present invention outside from the second diversion tube inside between make to have and be different spiral flows to the structure of spiral flow deflector, and/or the inside of the first diversion tube, make to have and be different spiral flows to the front view of spiral flow deflector embodiment;
Figure 14 shows that the side-looking generalized section of Figure 13 structure embodiment.
The specific embodiment
Hereby with regard to its main composition, be described as follows:
As Fig. 1 and Fig. 2, the present invention borrows fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes, its main composition is the first diversion tube 101 having more than a Huo Yi road, road, the first diversion tube 101 consists of heat carrier, and form the first stream 102 by the pore of the first diversion tube 101, confluxing through first respectively in the first stream 102 two ends, through first fluid import and export 104, the first Wen Nengti 105 for flow morphology enter and flow out again in chamber 103, and at the outside sheathed above internal diameter of tube body in Huo Yi road, road of the first diversion tube 101, be greater than the first diversion tube 101 external diameters and form the second diversion tube 201 and form two-layer pipe structure, the second diversion tube 201 consists of heat carrier, and by poor the second stream 202 for looping section of the caliber of the larger internal diameter of the second diversion tube 201 and the first diversion tube 101 external diameters, the second stream 202 two ends are imported and exported 204 through second fluid again and are entered and flow out for the second Wen Nengti 205 that is flow morphology through second chamber 203 of confluxing respectively, the skin that wherein forms the second diversion tube 201 is the fluid for being contacted with gaseous state or liquid state, or the 3rd Wen Nengti 305 being formed by solid-state Wen Nengti and then form be three temperature of shellring shape can body heat switches, for by the second Wen Nengti 205 and the first Wen Nengti 105 and and the 3rd Wen Nengti 305 threes between do the heat exchange that Wen Nengre passes,
Above-mentioned the first diversion tube 101, the second diversion tube 201 can be a Huo Yi road, road and form above;
Above-mentioned the first diversion tube 101, the second diversion tube 201 can be bodys round or square or ellipse or other geometries and form;
Above-mentioned the first diversion tube 101, the second diversion tube 201 can be identical shaped or difform body and form;
Above-mentioned the first Wen Nengti 105, the second Wen Nengti 205 can be identical or different fluid and form, and comprise that by gaseous state or liquid state or gaseous state, turning the liquid or liquid fluid that turns gaseous state is formed;
In above-mentioned the first diversion tube 101, supply institute in the first Wen Nengti 105 of circulation and the second diversion tube 201 to supply the flow direction of the second Wen Nengti 205 of circulating to can be identical or contrary.
The present invention borrows three temperature that fit multilayer pipe and the peripheral externally heat of pipeline passes can body heat switches, in the 3rd Wen Nengti 305, when consisting of gaseous state or fluid liquid, can further add fluid pump 400 and promote heat exchange effects with moving the 3rd Wen Nengti 305 of pump.
As shown in Fig. 3 and Fig. 4, for further adding fluid pump 400, with moving the 3rd Wen Nengti 305 of pump, promote heat exchange effect.
As shown in Fig. 5 and Fig. 6, between the second diversion tube 201 in Fig. 1, Fig. 2 embodiment, heat conduction fin 1000 being further set, for the second diversion tube 201 and the 3rd Wen Nengti 305 intercropping temperature, can conduct.
The present invention borrows fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes, its first diversion tube 101 and the second diversion tube 201, except being parallel connection by each pipeline section as shown in Figure 1 and Figure 2, are further cascaded structure by the first diversion tube 101 and the second diversion tube 201; Hereby be described as follows:
As shown in Fig. 7 and Fig. 8, for by Fig. 1, the first diversion tube 101 in Fig. 2 embodiment is series connection, each pipeline section of the second diversion tube 201 is made and is connected in series, the first diversion tube 101 consists of heat carrier, the first stream 102 is connected with the first stream 102 of at least one the first diversion tube 101 through first chamber 103 of confluxing, by the first stream 102 two ends after series connection, lead to respectively first fluid again and import and export 104, use the first Wen Nengti 105 for flow morphology enter and flow out, and the two-layer pipe structure of the second diversion tube 201 formation that is greater than the first diversion tube 101 external diameters at the outside sheathed internal diameter of tube body of the first diversion tube 101, the second diversion tube 201 consists of heat carrier, and by poor the second stream 202 for looping section of the caliber of the larger internal diameter of the second diversion tube 201 and the first diversion tube 101 external diameters, the second stream 202 is connected with the second stream 202 of at least one the second diversion tube 201 through second chamber 203 of confluxing, by the second stream 202 two ends after series connection, lead to respectively second fluid again and import and export 204, use for the second Wen Nengti 205 that is flow morphology and enter and flow out, the skin that wherein forms the second diversion tube 201 is the fluid for being contacted with gaseous state or liquid state, or the 3rd Wen Nengti 305 being formed by solid-state Wen Nengti and then form be three temperature of shellring shape can body heat switches, for by the second Wen Nengti 205 and the first Wen Nengti 105 and and the 3rd Wen Nengti 305 threes between do the heat exchange that Wen Nengre passes.
As shown in Fig. 9 and Figure 10, for the first diversion tube 101 in Fig. 5, Fig. 6 embodiment and each pipeline section of being coated on the second diversion tube 201 of the first diversion tube 101 outsides are made and be connected in series.
The present invention borrows fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes, further for making the structure with spiral flow deflector 222 between the first diversion tube 101 is outside and the second diversion tube 201 inside, and/or the inside of the first diversion tube 101, make the structure with spiral flow deflector 111 and pass effect to increase heat, be hereby described as follows:
As shown in Figure 11 and Figure 12, wherein for forming the present invention, borrow to make to have between outside and the second diversion tube 201 inside of the first diversion tube 101 that three temperature that fit multilayer pipe and the peripheral externally heat of pipeline passes can body heat switches and be same spiral flow to the structure of spiral flow deflector 222, and/or the inside of the first diversion tube 101, make to have and be same spiral flow to the structure of spiral flow deflector 111.
As shown in Figure 13 and Figure 14, wherein for form the present invention borrow the first diversion tube 101 that three temperature that fit multilayer pipe and the peripheral externally heat of pipeline passes can body heat switches outside from the second diversion tube 201 inside between make to have and be different spiral flows to the structure of spiral flow deflector 222, and/or the inside of the first diversion tube 101, make to have and be different spiral flows to the structure of spiral flow deflector 111.
The above embodiment is only the preferred embodiment for absolutely proving that the present invention lifts, and protection scope of the present invention is not limited to this.Being equal to that those skilled in the art do on basis of the present invention substitutes or conversion, all within protection scope of the present invention.Protection scope of the present invention is as the criterion with claims.
Claims (14)
1. borrow fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes for one kind, it is characterized in that: its main composition is the first diversion tube (101) having more than a Huo Yi road, road, the first diversion tube (101) consists of heat carrier, and form the first stream (102) by the pore of the first diversion tube (101), confluxing through first respectively in the first stream (102) two ends, through first fluid import and export (104), the first Wen Nengti (105) for flow morphology enters and flows out again in chamber (103), and at the outside sheathed above internal diameter of tube body in Huo Yi road, road of the first diversion tube (101), be greater than the first diversion tube (101) external diameter and form the second diversion tube (201) and form two-layer pipe structure, the second diversion tube (201) consists of heat carrier, and by poor the second stream (202) for looping section of the caliber of the larger internal diameter of the second diversion tube (201) and the first diversion tube (101) external diameter, the second stream (202) two ends are imported and exported (204) through second fluid again and are entered and flow out for the second Wen Nengti (205) that is flow morphology through second chamber (203) of confluxing respectively, the skin that wherein forms the second diversion tube (201) is the fluid for being contacted with gaseous state or liquid state, or the 3rd Wen Nengti (305) being formed by solid-state Wen Nengti and then form be three temperature of shellring shape can body heat switches, for by the second Wen Nengti (205) and the first Wen Nengti (105) and and the 3rd Wen Nengti (305) three between do the heat exchange that Wen Nengre passes.
2. as claimed in claim 1 by means of fit multilayer pipe and the pipeline periphery three warm energy body heat switches that externally heat passes, it is characterized in that: further comprise the first diversion tube (101), by heat carrier, formed, the first stream (102) is connected with first stream (102) of at least one the first diversion tube (101) through first chamber (103) of confluxing, by the first stream (102) two ends after series connection, lead to respectively first fluid again and import and export (104), use the first Wen Nengti (105) for flow morphology enter and flow out, and form two-layer pipe structure at the second diversion tube (201) that the outside sheathed internal diameter of tube body of the first diversion tube (101) is greater than the first diversion tube (101) external diameter, the second diversion tube (201) consists of heat carrier, and by poor the second stream (202) for looping section of the caliber of the larger internal diameter of the second diversion tube (201) and the first diversion tube (101) external diameter, the second stream (202) is connected with second stream (202) of at least one the second diversion tube (201) through second chamber (203) of confluxing, by the second stream (202) two ends after series connection, lead to respectively second fluid again and import and export (204), use for the second Wen Nengti (205) that is flow morphology and enter and flow out, the skin that wherein forms the second diversion tube (201) is the fluid for being contacted with gaseous state or liquid state, or the 3rd Wen Nengti (305) being formed by solid-state Wen Nengti and then form be three temperature of shellring shape can body heat switches, for by the second Wen Nengti (205) and the first Wen Nengti (105) and and the 3rd Wen Nengti (305) three between do the heat exchange that Wen Nengre passes.
3. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 1 or 2, is characterized in that: described the first diversion tube (101), the second diversion tube (201) can be bodys round or square or ellipse or other geometries and form.
4. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 1 or 2, is characterized in that: described the first diversion tube (101), the second diversion tube (201) are formed by identical shaped or difform body.
5. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 1 or 2, is characterized in that: described the first Wen Nengti (105), the second Wen Nengti (205) are formed by identical or different fluid.
6. the three temperature energy body heat switches of borrowing the external heat of fit multilayer pipe and pipeline periphery to pass as claimed in claim 1 or 2, is characterized in that: described fluid comprises by gas or liquid or gaseous state turns liquid state or the liquid fluid that turns gaseous state is formed.
7. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 1 or 2, is characterized in that: described the 3rd Wen Nengti (305) is containing being consisted of fluid or solid.
8. as claimed in claim 1 or 2 by means of fit multilayer pipe and the pipeline periphery three warm energy body heat switches that externally heat passes, it is characterized in that: described the 3rd Wen Nengti (305) when consisting of fluid, can further add fluid pump (400) and promote heat exchange effect with moving the 3rd Wen Nengti (305) of pump.
9. as claimed in claim 1 or 2ly borrow three temperature that fit multilayer pipe and the peripheral externally heat of pipeline passes can body heat switches, it is characterized in that: in described the first diversion tube (101), supply first Wen Nengti (105) of circulation and the second diversion tube (201) middle to supply the flow direction of the second Wen Nengti (205) of circulating be identical or contrary.
10. as claimed in claim 1 or 2 by means of fit multilayer pipe and the pipeline periphery three warm energy body heat switches that externally heat passes, it is characterized in that: described fit multilayer pipe comprises by two-layer or two-layer above heat carrier and forming, and form relative number object diversion tube, for supplying by identical or different fluid in each body, its direction of flow that is fit adjacent tubes interlayer different fluid pipeline is identical or contrary.
11. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 1 or 2, is characterized in that: heat conduction fin (1000) is further set between described the second diversion tube (201).
12. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 1 or 2, it is characterized in that: further for making the there is spiral flow deflector structure of (222) between the first diversion tube (101) is outside and the second diversion tube (201) inside, and/or the inside of the first diversion tube (101), make and there is spiral flow deflector the structure of (111) passes effect to increase heat.
13. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 12, it is characterized in that: between outside and the second diversion tube (201) inside of described the first diversion tube (101), make to have and be same spiral flow to the structure of spiral flow deflector (222), and/or the inside of the first diversion tube (101), make to have and be same spiral flow to the structure of spiral flow deflector (111).
14. fit multilayer pipe and the pipeline periphery three temperature energy body heat switches that externally heat passes of borrowing as claimed in claim 12, it is characterized in that: described the first diversion tube (101) outside from the second diversion tube (201) inside between make to have and be different spiral flows to the structure of spiral flow deflector (222), and/or the inside of the first diversion tube (101), make to have and be different spiral flows to the structure of spiral flow deflector (111).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910500868.0A CN110274494A (en) | 2012-09-27 | 2013-09-27 | By means of fitting multilayer pipe and the pipeline periphery three thermal energy body heat-exchange devices that externally heat passes |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| 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 |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910500868.0A Division CN110274494A (en) | 2012-09-27 | 2013-09-27 | By means of fitting multilayer pipe and the pipeline periphery three thermal energy body heat-exchange devices that externally heat passes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103697725A true CN103697725A (en) | 2014-04-02 |
Family
ID=49328337
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310448066.2A Pending CN103697725A (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 |
| CN201320600892.XU Expired - Lifetime CN203501858U (en) | 2012-09-27 | 2013-09-27 | Tree-temperature-energy-body heat exchange device for transferring heat outside by being sleeved with multilayered pipes and pipe periphery |
| CN201910500868.0A Pending CN110274494A (en) | 2012-09-27 | 2013-09-27 | By means of fitting multilayer pipe and the pipeline periphery three thermal energy body heat-exchange devices that externally heat passes |
Family Applications After (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320600892.XU Expired - Lifetime CN203501858U (en) | 2012-09-27 | 2013-09-27 | Tree-temperature-energy-body heat exchange device for transferring heat outside by being sleeved with multilayered pipes and pipe periphery |
| CN201910500868.0A Pending CN110274494A (en) | 2012-09-27 | 2013-09-27 | By means of fitting multilayer pipe and the pipeline periphery three thermal energy body heat-exchange devices that externally heat passes |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20140083666A1 (en) |
| EP (1) | EP2713131B1 (en) |
| JP (2) | JP6401439B2 (en) |
| CN (3) | CN103697725A (en) |
| AU (2) | AU2013234402B2 (en) |
| CA (1) | CA2828311C (en) |
| SG (1) | SG2013073028A (en) |
| TW (3) | TWI619922B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105972869A (en) * | 2016-06-14 | 2016-09-28 | 杨胜东 | Dual-purpose large-channel heat exchanger for evaporation and condensation and system thereof |
| 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 |
Families Citing this family (5)
| 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 |
| WO2019240156A1 (en) * | 2018-06-12 | 2019-12-19 | 株式会社Ihi | 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 |
| CZ2020146A3 (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 (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2094021U (en) * | 1991-05-25 | 1992-01-22 | 程效民 | Tube in tube tubular heat-exchanger |
| CN200947001Y (en) * | 2006-04-30 | 2007-09-12 | 华南理工大学 | Sleeve-type heat exchanger |
| CN101105373A (en) * | 2007-08-01 | 2008-01-16 | 中原工学院 | Fin-sleeve type three mediums composite 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 |
| 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 |
| CN203501858U (en) * | 2012-09-27 | 2014-03-26 | 杨泰和 | Tree-temperature-energy-body heat exchange device for transferring heat outside by being sleeved with multilayered pipes and pipe periphery |
Family Cites Families (27)
| 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 |
| DE8409717U1 (en) * | 1984-03-27 | 1986-11-20 | Schick, Josef Hubert, 5203 Much | Device for heat and mass exchange between two or more flowing 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 |
| 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 |
| TW495013U (en) * | 2001-12-04 | 2002-07-11 | Taiwan Reduce Pollutant Techno | 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 |
| WO2008078194A2 (en) * | 2006-06-20 | 2008-07-03 | Adir Segal, Ltd. | Thermal load management system |
| DE102007054703B4 (en) * | 2007-11-14 | 2012-04-19 | GEA Luftkühler GmbH | heat exchangers |
| JP2009162395A (en) * | 2007-12-28 | 2009-07-23 | Showa Denko Kk | Double-wall-tube heat exchanger |
| TWM396600U (en) * | 2009-10-16 | 2011-01-21 | Tai-Her Yang | Heat absorbing or disspating device with piping staggered and uniformly distributed by 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 |
-
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 AU AU2013234402A patent/AU2013234402B2/en active Active
- 2013-09-27 EP EP13186548.7A patent/EP2713131B1/en active Active
- 2013-09-27 CN CN201310448066.2A patent/CN103697725A/en active Pending
- 2013-09-27 TW TW106115210A patent/TWI619922B/en active
- 2013-09-27 TW TW102218081U patent/TWM476252U/en not_active IP Right Cessation
- 2013-09-27 SG SG2013073028A patent/SG2013073028A/en unknown
- 2013-09-27 TW TW102134914A patent/TWI586932B/en active
- 2013-09-27 CN CN201320600892.XU patent/CN203501858U/en not_active Expired - Lifetime
- 2013-09-27 JP JP2013200948A patent/JP6401439B2/en active Active
- 2013-09-27 CN CN201910500868.0A patent/CN110274494A/en active Pending
-
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 (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2094021U (en) * | 1991-05-25 | 1992-01-22 | 程效民 | Tube in tube tubular heat-exchanger |
| CN200947001Y (en) * | 2006-04-30 | 2007-09-12 | 华南理工大学 | Sleeve-type heat exchanger |
| CN101105373A (en) * | 2007-08-01 | 2008-01-16 | 中原工学院 | Fin-sleeve type three mediums composite 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 |
| 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 |
| CN203501858U (en) * | 2012-09-27 | 2014-03-26 | 杨泰和 | Tree-temperature-energy-body heat exchange device for transferring heat outside by being sleeved with multilayered pipes and pipe periphery |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105972869A (en) * | 2016-06-14 | 2016-09-28 | 杨胜东 | Dual-purpose large-channel heat exchanger for evaporation and condensation and system thereof |
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| SG2013073028A (en) | 2014-04-28 |
| AU2013234402A1 (en) | 2014-04-10 |
| TW201730495A (en) | 2017-09-01 |
| AU2017268511A1 (en) | 2017-12-14 |
| AU2013234402A2 (en) | 2017-03-02 |
| CA2828311C (en) | 2020-07-28 |
| JP2014074581A (en) | 2014-04-24 |
| TWI619922B (en) | 2018-04-01 |
| CN203501858U (en) | 2014-03-26 |
| JP6401439B2 (en) | 2018-10-10 |
| EP2713131B1 (en) | 2016-06-08 |
| CN110274494A (en) | 2019-09-24 |
| TWM476252U (en) | 2014-04-11 |
| TW201416638A (en) | 2014-05-01 |
| JP6746647B2 (en) | 2020-08-26 |
| AU2013234402B2 (en) | 2017-09-21 |
| CA2828311A1 (en) | 2014-03-27 |
| US20140083666A1 (en) | 2014-03-27 |
| JP2019007729A (en) | 2019-01-17 |
| EP2713131A1 (en) | 2014-04-02 |
| TWI586932B (en) | 2017-06-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203501858U (en) | Tree-temperature-energy-body heat exchange device for transferring heat outside by being sleeved with multilayered pipes and pipe periphery | |
| US10119769B2 (en) | Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline | |
| CN201688738U (en) | Thermal conductive column with internal U-shaped core tube and ring tube | |
| CN202675974U (en) | Pipe body with central heat-insulating pipelines and U-shaped circularly-distributed pipelines | |
| CN203534312U (en) | Pipe body with core heat-insulating pipeline, auxiliary heat conduction structure and U-shaped annularly-distributed pipeline | |
| CN104374098A (en) | Vacuum tube solar heat collector | |
| CN208443241U (en) | A kind of heat exchange-heat-storing device | |
| CN201096399Y (en) | Liquid-heating device | |
| CN203534314U (en) | H-shaped nickel alloy brazing finned tube | |
| CN203848524U (en) | Solar energy photo-thermal utilizing device | |
| CN203349484U (en) | Hot water generation device | |
| CN206944531U (en) | Heat exchanger and hot water supply system | |
| CN207066199U (en) | Shell-and-tube exchanger | |
| CN202254310U (en) | Combined type spiral metal bellows heat exchanger | |
| CN203848534U (en) | Heat exchanger used for solar energy photo-thermal utilizing device | |
| CN204285850U (en) | A kind of vacuum tube solar heating element | |
| CN105422227B (en) | Heat transfer and the tandem type vehicle exhaust heat-exchanger rig of thermoradiation efficiency superposition | |
| CN203069025U (en) | Spiral heat exchange pipe | |
| CN203772065U (en) | Casing pipe type heat exchanger | |
| CN206556463U (en) | Heat exchanger with pipeline staggered structure | |
| CN103868251B (en) | A kind of heat exchanger in solar energy heat utilization device | |
| CN105129264A (en) | Multilayer cylindrical spiral pipe solar storage tank | |
| CN105300144A (en) | Efficient heat transferring and exchange device | |
| CN103486888A (en) | Depth heat exchanger |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20140402 |