CN106764128A - A kind of gas liquid two purpose spiral temperature control flow tube - Google Patents
A kind of gas liquid two purpose spiral temperature control flow tube Download PDFInfo
- Publication number
- CN106764128A CN106764128A CN201611146512.4A CN201611146512A CN106764128A CN 106764128 A CN106764128 A CN 106764128A CN 201611146512 A CN201611146512 A CN 201611146512A CN 106764128 A CN106764128 A CN 106764128A
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- Prior art keywords
- level
- deflector
- order
- temperature control
- control flow
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L9/00—Rigid pipes
- F16L9/18—Double-walled pipes; Multi-channel pipes or pipe assemblies
- F16L9/19—Multi-channel pipes or pipe assemblies
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L55/00—Devices or appurtenances for use in, or in connection with, pipes or pipe systems
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- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a kind of gas liquid two purpose spiral temperature control flow tube, including：Outer tube body and the interior tube body being arranged inside outer tube body；Interior tube body includes：First order body, second level body and third level body；First order pipe diameter is less than second level pipe diameter, and second level pipe diameter is less than third level pipe diameter；Second level body is fixed on first order body output end；Third level body is fixed on second level body output end；The outer wall of first order body and the outer wall of second level body are provided with helical blade；The first order body port of export is provided with the deflector being upwardly directed；Using the present invention of above-mentioned technical proposal, the gas or liquid of the tube chamber conveying of interior tube body are oriented to by the unhurried current of deflector, then slow down by the multistage caliber that increases, while gap is gradually reduced between outer tube body and interior tube body, realize speedup, and then realize heat exchange balance.
Description
Technical field
The present invention relates to delivery pipe field, more particularly to a kind of gas liquid two purpose spiral temperature control flow tube.
Background technology
At present, delivery pipe function is relatively simple, is generally only conveying gas or liquid；
And with industrial expansion, for the increase of supply also feed flow requirement, generally require the gas-liquid of uniform temperature simultaneously
Injection；
At present can only be real in the case where carrying out Insulation or providing extra heater by two independent pipelines
It is existing.
The content of the invention
The present invention is directed to above-mentioned technical problem, proposes that one kind can simultaneously separate conveying gas and liquid, while gas and liquid
Body possesses heat-exchange time and space in course of conveying, realizes that temperature control is conveyed.
To achieve the above objectives, it is achieved through the following technical solutions：
A kind of gas liquid two purpose spiral temperature control flow tube, including：Outer tube body and the interior tube body being arranged inside outer tube body；
Interior tube body includes：First order body, second level body and third level body；
First order pipe diameter is less than second level pipe diameter, and second level pipe diameter is less than third level pipe diameter；
Second level body is fixed on first order body output end；
Third level body is fixed on second level body output end；
The outer wall of first order body and the outer wall of second level body are provided with helical blade.
The first order body port of export is provided with the deflector I being upwardly directed.
Deflector is arc deflector.
Along the deflector II being directed downwardly toward is provided with the body port of export of the second level, port of export lower edge is provided with and is upwardly directed
Deflector III, and the diameter width more than or equal to 1/2nd second level bodys is provided between deflector II and deflector III
Gap.
Deflector II and deflector III are arc deflector.
Using the present invention of above-mentioned technical proposal, the tube chamber one formed between the tube chamber and outer tube body and interior tube body of interior tube body
It is individual for conveying liquid, another be used for convey gas；
It is assumed that now interior tube body conveying gas, the tube chamber conveying liquid formed between outer tube body and interior tube body；
So gas forms eddy flow and is oriented in the outlet port of first order body by deflector I, enters into greater room
Second level body in, flow velocity is also reduced, so gas to form many vortex residence times in second level body more long, now
Helical blade spiral pile warp first order body and second level body that liquid passes through first order tube wall, due to second level body
Diameter is greater than gap between first order body, and then second level body and outer tube body and diminishes, then liquid can be managed in the second level
Speedup in body section official jargon, and because gas residence time in fact is long, then ensure that first order body and second level body
Heat exchange efficiency is identical；
Gas is oriented in the second level body port of export by deflector II and deflector III, and being now oriented to can occur mutually to rush,
At this moment can cause gas turbulence, but due in the chamber for entering into bigger third level body flow velocity further reduce, then
Very many vortex can be formed, gas residence time is most long；Simultaneously because third level pipe diameter is managed more than the second level
Body diameter, causes tube chamber between third level body and outer tube body minimum, the further speedup of flow rate of liquid, now further through gas
Main flow ensures the balance of heat exchange efficiency often.
Described above is only the general introduction of technical solution of the present invention, in order to better understand technological means of the invention,
And can be practiced according to the content of specification, and in order to allow the above and other objects, features and advantages of the invention can
Become apparent, below especially exemplified by preferred embodiment, and coordinate accompanying drawing, describe in detail as follows.
Brief description of the drawings
Totally 1 width accompanying drawing of the invention, wherein：
Fig. 1 is overall structure diagram of the invention.
In figure：1st, outer tube body, 2, interior tube body, 2.1, first order body, 2.11, deflector I, 2.2, second level body,
2.21st, deflector II, 2.22, deflector III, 2.3, third level body 2.3,3, helical blade.
Specific embodiment
A kind of gas liquid two purpose spiral temperature control flow tube as shown in Figure 1, including：Outer tube body 1 and it is arranged inside outer tube body 1
Interior tube body 2；
Interior tube body 2 includes：First order body 2.1, second level body 2.2 and third level body 2.3；
The diameter of first order body 2.1 is less than the diameter of second level body 2.2, and the diameter of second level body 2.2 is less than third level
The diameter of body 2.3；
Second level body 2.2 is fixed on the output end of first order body 2.1；
Third level body 2.3 is fixed on the output end of second level body 2.2；
The outer wall of first order body 2.1 and the outer wall of second level body 2.2 are provided with helical blade 3.
The port of export of first order body 2.1 is provided with the deflector I 2.11 being upwardly directed.
Deflector 2.11 is arc deflector.
Along the deflector II 2.21 being directed downwardly toward is provided with the port of export of second level body 2.2, port of export lower edge is provided with
The deflector III 2.22 being upwardly directed, and be provided with more than or equal to 1/2nd between deflector II 2.21 and deflector III 2.22
The gap of the diameter width of second level body 2.2.
Deflector II 2.21 and deflector III 2.22 are arc deflector.
Using the present invention of above-mentioned technical proposal, the pipe formed between the tube chamber and outer tube body 1 and interior tube body 2 of interior tube body 2
One, chamber is used for conveying liquid, and another is used for conveying gas；
It is assumed that the now conveying of interior tube body 2 gas, the tube chamber conveying liquid formed between outer tube body 1 and interior tube body 2；
So gas forms eddy flow and is oriented in the outlet port of first order body 2.1 by deflector I 2.11, enters into more
In the second level body 2.2 of large space, flow velocity is also reduced, and then gas can form many vortex and be resident in second level body 2.2
Time is more long, the spiral pile warp first order body 2.1 and second of helical blade 3 that now liquid passes through the outer wall of first order body 2.1
Level body 2.2, because the diameter of second level body 2.2 is greater than first order body 2.1, and then second level body 2.2 and outer tube body 1
Between gap diminish, then liquid can in 2.2 sections of official jargons of the second level body speedup, and due to gas residence time in fact
It is long, then to ensure that first order body 2.1 is identical with the heat exchange efficiency of second level body 2.2；
Gas is oriented in the port of export of second level body 2.2 by deflector II 2.21 and deflector III 2.22, is now oriented to
Can occur mutually to rush, at this moment can cause gas turbulence, but due in the chamber for entering into bigger third level body 2.3 flow velocity enter
One step reduction, then very many vortex can be formed, gas residence time is most long；Simultaneously due to third level body 2.3
With diameter greater than the diameter of second level body 2.2, tube chamber minimum between third level body 2.3 and outer tube body 1 is caused, flow rate of liquid enters
One step speedup, now ensures the balance of heat exchange efficiency often further through main flow of gas.
The above, is only presently preferred embodiments of the present invention, and any formal limitation is not made to the present invention, though
So the present invention is disclosed above with preferred embodiment, but is not limited to the present invention, any to be familiar with this professional technology people
Member without departing from the scope of the present invention, when using the technology contents of the disclosure above make it is a little change or be modified to
The Equivalent embodiments of equivalent variations, as long as being the content without departing from technical solution of the present invention, according to technical spirit pair of the invention
Any simple modification made for any of the above embodiments, equivalent variations and modification, still fall within the range of technical solution of the present invention.
Claims (5)
1. a kind of gas liquid two purpose spiral temperature control flow tube, it is characterised in that including：Outer tube body (1) and to be arranged at outer tube body (1) internal
Interior tube body (2)；
Said inner tube body (2) includes：First order body (2.1), second level body (2.2) and third level body (2.3)；
First order body (2.1) diameter is less than second level body (2.2) diameter, and second level body (2.2) diameter is less than the
Three-level don't bother about body (2.3) diameter；
The second level body (2.2) is fixed on first order body (2.1) output end；
The third level body (2.3) is fixed on second level body (2.2) output end；
The outer wall of the first order body (2.1) and the outer wall of second level body (2.2) are provided with helical blade (3).
2. a kind of gas liquid two purpose spiral temperature control flow tube according to claim 1, it is characterised in that：
First order body (2.1) port of export is provided with the deflector I (2.11) being upwardly directed.
3. a kind of gas liquid two purpose spiral temperature control flow tube according to claim 2, it is characterised in that：The deflector (2.11)
It is arc deflector.
4. a kind of gas liquid two purpose spiral temperature control flow tube according to claim 1, it is characterised in that：The second level body
(2.2) along the deflector II (2.21) being directed downwardly toward is provided with the port of export, port of export lower edge is provided with the water conservancy diversion being upwardly directed
It is provided between plate III (2.22), and deflector II (2.21) and deflector III (2.22) and is managed more than or equal to 1/2nd second level
The gap of the diameter width of body (2.2).
5. a kind of gas liquid two purpose spiral temperature control flow tube according to claim 4, it is characterised in that：Deflector II (2.21) and
Deflector III (2.22) is arc deflector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611146512.4A CN106764128B (en) | 2016-12-13 | 2016-12-13 | A kind of gas liquid two purpose spiral temperature control flow tube |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611146512.4A CN106764128B (en) | 2016-12-13 | 2016-12-13 | A kind of gas liquid two purpose spiral temperature control flow tube |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106764128A true CN106764128A (en) | 2017-05-31 |
| CN106764128B CN106764128B (en) | 2019-03-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611146512.4A Active CN106764128B (en) | 2016-12-13 | 2016-12-13 | A kind of gas liquid two purpose spiral temperature control flow tube |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2413258Y (en) * | 1999-05-24 | 2001-01-03 | 上海得灵电器实业有限公司 | Spiral heat-transfer tube |
| CN2510814Y (en) * | 2001-12-26 | 2002-09-11 | 台湾雷德斯减废科技有限公司 | Heat exchanger |
| CN201293586Y (en) * | 2008-08-22 | 2009-08-19 | 湖南晟通科技集团有限公司 | Highly effective heat exchange tube |
| CN201653004U (en) * | 2010-01-19 | 2010-11-24 | 梁立仕 | Reducing pipe water-cooled condenser for air conditioner |
| CN102313466A (en) * | 2011-09-09 | 2012-01-11 | 珠海亚必利科技有限公司 | Heat exchanger with reducer pipeline |
| US20160282052A1 (en) * | 2015-03-12 | 2016-09-29 | Milton Edward Vernon | Nested-Flow Heat Exchangers and Chemical Reactors |
-
2016
- 2016-12-13 CN CN201611146512.4A patent/CN106764128B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2413258Y (en) * | 1999-05-24 | 2001-01-03 | 上海得灵电器实业有限公司 | Spiral heat-transfer tube |
| CN2510814Y (en) * | 2001-12-26 | 2002-09-11 | 台湾雷德斯减废科技有限公司 | Heat exchanger |
| CN201293586Y (en) * | 2008-08-22 | 2009-08-19 | 湖南晟通科技集团有限公司 | Highly effective heat exchange tube |
| CN201653004U (en) * | 2010-01-19 | 2010-11-24 | 梁立仕 | Reducing pipe water-cooled condenser for air conditioner |
| CN102313466A (en) * | 2011-09-09 | 2012-01-11 | 珠海亚必利科技有限公司 | Heat exchanger with reducer pipeline |
| US20160282052A1 (en) * | 2015-03-12 | 2016-09-29 | Milton Edward Vernon | Nested-Flow Heat Exchangers and Chemical Reactors |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106764128B (en) | 2019-03-26 |
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Effective date of registration: 20210528 Address after: No.18-91, Gongye Road, South Taihu high tech Industrial Park, Wuxing District, Huzhou City, Zhejiang Province Patentee after: Zhejiang julibao Textile Technology Co., Ltd Address before: 116000 -B 8, Liaohe three road, Jinzhou New District, Dalian, Liaoning. Patentee before: DEVELOPMENT DISTRICT BRANCH COMPANY, DALIAN SHENGJIE VACUUM TECHNOLOGY DEVELOPMENT Co.,Ltd. |