CN106764128B - 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
- CN106764128B CN106764128B CN201611146512.4A CN201611146512A CN106764128B CN 106764128 B CN106764128 B CN 106764128B CN 201611146512 A CN201611146512 A CN 201611146512A CN 106764128 B CN106764128 B CN 106764128B
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- tube body
- level
- deflector
- order
- gas
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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 tubes, comprising: outer tube body and the interior tube body being set to inside outer tube body；Interior tube body includes: first order tube body, second level tube body and third level tube 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 tube body is fixed on first order tube body output end；Third level tube body is fixed on second level tube body output end；The outer wall of first order tube body and the outer wall of second level tube body are provided with helical blade；First order tube body outlet end is provided with the deflector being upwardly directed；The present invention by adopting the above technical scheme, the gas or liquid of the lumen conveying of interior tube body are oriented to by the unhurried current of deflector, increase caliber using multistage and slow down, 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, in particular to a kind of gas liquid two purpose spiral temperature control flow tube.
Background technique
Currently, delivery pipe function is relatively simple, it is generally only conveying gas or liquid；
And with the development of industry, for supplying the increase that also feed flow requires, generally require the gas-liquid of certain temperature simultaneously
Injection；
It at present can only be real in the case where carrying out Insulation or providing additional heating device by two independent pipelines
It is existing.
Summary of the invention
The present invention in view of the above technical problems, proposes that one kind can separate conveying gas and liquid, while gas and liquid simultaneously
Body possesses heat-exchange time and space during transportation, realizes temperature control conveying.
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, comprising: outer tube body and the interior tube body being set to inside outer tube body；
Interior tube body includes: first order tube body, second level tube body and third level tube 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 tube body is fixed on first order tube body output end；
Third level tube body is fixed on second level tube body output end；
The outer wall of first order tube body and the outer wall of second level tube body are provided with helical blade.
First order tube body outlet end is provided with the deflector I being upwardly directed.
Deflector is arc deflector.
Along the deflector II being directed downwardly toward is provided on the tube body outlet end of the second level, outlet end lower edge, which is provided with, to be upwardly directed
Deflector III, and the diameter width more than or equal to half second level tube body is provided between deflector II and deflector III
Gap.
Deflector II and deflector III are arc deflector.
The present invention by adopting the above technical scheme, the lumen one formed between the lumen and outer tube body and interior tube body of interior tube body
A to be used to convey liquid, another is used to convey gas；
It is assumed that interior tube body conveys gas at this time, the lumen conveying liquid formed between outer tube body and interior tube body；
So gas forms eddy flow guiding by deflector I in the outlet port of first order tube body, enters greater room
Second level tube body in, flow velocity also reduces, and then to form many vortex residence times in second level tube body longer for gas, at this time
Liquid passes through the helical blade spiral pile warp first order tube body and second level tube body of first order tube wall, due to second level tube body
Diameter is greater than first order tube body, and then gap becomes smaller between second level tube body and outer tube body, then liquid can be managed in the second level
Speedup in body section official jargon, and since gas residence time in fact is long, then ensuring that first order tube body and second level tube body
Heat exchange efficiency is identical；
Gas is oriented in second level tube body outlet end by deflector II and deflector III, and guiding can occur mutually to rush at this time,
At this moment it will cause gas turbulence, and flow velocity further decreases in the chamber due to entering bigger third level tube body, then
It will form very more vortex, gas residence time longest；Simultaneously managed due to third level pipe diameter greater than the second level
Body diameter causes lumen between third level tube body and outer tube body minimum, the further speedup of flow rate of liquid, at this time further through gas
Mainstream guarantees the balance of heat exchange efficiency often.
The above description is only an overview of the technical scheme of the present invention, in order to better understand the technical means of the present invention,
And it can be implemented in accordance with the contents of the specification, and in order to allow above and other objects, features and advantages of the invention can
It is clearer and more comprehensible, it is special below to lift preferred embodiment, and cooperate attached drawing, detailed description are as follows.
Detailed description of the invention
The present invention totally 1 width attached drawing, wherein:
Fig. 1 is overall structure diagram of the invention.
In figure: 1, outer tube body, 2, interior tube body, 2.1, first order tube body, 2.11, deflector I, 2.2, second level tube body,
2.21, deflector II, 2.22, deflector III, 2.3, third level tube 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, comprising: outer tube body 1 and be set to inside outer tube body 1
Interior tube body 2；
Interior tube body 2 includes: first order tube body 2.1, second level tube body 2.2 and third level tube body 2.3；
2.1 diameter of first order tube body is less than 2.2 diameter of second level tube body, and tube body 2.2 diameter in the second level is less than third level
2.3 diameter of tube body；
Second level tube body 2.2 is fixed on 2.1 output end of first order tube body；
Third level tube body 2.3 is fixed on 2.2 output end of second level tube body；
The outer wall of first order tube body 2.1 and the outer wall of second level tube body 2.2 are provided with helical blade 3.
2.1 outlet end of first order tube body 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 on 2.2 outlet end of second level tube body, outlet end lower edge is provided with
The deflector III 2.22 being upwardly directed, and be provided between deflector II 2.21 and deflector III 2.22 more than or equal to half
The gap of the diameter width of second level tube body 2.2.
Deflector II 2.21 and deflector III 2.22 are arc deflector.
The present invention by adopting the above technical scheme, the pipe formed between the lumen and outer tube body 1 and interior tube body 2 of interior tube body 2
One, chamber is used to convey liquid, another is used to convey gas；
It is assumed that interior tube body 2 conveys gas at this time, the lumen conveying liquid formed between outer tube body 1 and interior tube body 2；
So gas forms eddy flow guiding by deflector I 2.11 in the outlet port of first order tube body 2.1, enters more
In the second level tube body 2.2 of large space, flow velocity is also reduced, and then gas can form many vortex in second level tube body 2.2 and be resident
Time is longer, and liquid passes through the 3 spiral pile warp first order tube body 2.1 and second of helical blade of 2.1 outer wall of first order tube body at this time
Grade tube body 2.2, since tube body 2.2 diameter in the second level is greater than first order tube body 2.1, and then second level tube body 2.2 and outer tube body 1
Between gap become smaller, then liquid can in 2.2 sections of official jargons of the second level tube body speedup, and due to gas residence time in fact
It is long, then ensuring that first order tube body 2.1 is identical with the heat exchange efficiency of second level tube body 2.2；
Gas is oriented in 2.2 outlet end of second level tube body by deflector II 2.21 and deflector III 2.22, is oriented at this time
Can occur mutually to rush, at this moment will cause gas turbulence, but in the chamber due to entering bigger third level tube body 2.3 flow velocity into
One step reduces, then will form very more vortex, gas residence time longest；Simultaneously due to third level tube body 2.3
Diameter is greater than 2.2 diameter of second level tube body, causes between third level tube body 2.3 and outer tube body 1 lumen minimum, flow rate of liquid into
One step speedup, guarantees the balance of heat exchange efficiency often further through main flow of gas at this time.
The above described is only a preferred embodiment of the present invention, be not intended to limit the present invention in any form, though
So the present invention has been disclosed as a preferred embodiment, and however, it is not intended to limit the invention, any technology people for being familiar with this profession
Member without departing from the scope of the present invention, when the technology contents using the disclosure above are modified or are modified to
The equivalent embodiment of equivalent variations, but anything that does not depart from the technical scheme of the invention content, it is right according to the technical essence of the invention
Any simple modification, equivalent change and modification made for any of the above embodiments, all of which are still within the scope of the technical scheme of the invention.
Claims (1)
1. a kind of gas liquid two purpose spiral temperature control flow tube characterized by comprising outer tube body (1) and to be set to outer tube body (1) internal
Interior tube body (2)；
Said inner tube body (2) includes: first order tube body (2.1), second level tube body (2.2) and third level tube body (2.3)；
First order tube body (2.1) diameter is less than second level tube body (2.2) diameter, and tube body (2.2) diameter in the second level is less than the
Three-level tube body (2.3) diameter；
The second level tube body (2.2) is fixed on first order tube body (2.1) output end；
The third level tube body (2.3) is fixed on second level tube body (2.2) output end；
The outer wall of the first order tube body (2.1) and the outer wall of second level tube body (2.2) are provided with helical blade (3)；
First order tube body (2.1) outlet end is provided with the deflector I (2.11) being upwardly directed；
The deflector I (2.11) is arc deflector；
Along the deflector II (2.21) being directed downwardly toward is provided on second level tube body (2.2) outlet end, outlet end lower edge is set
Be equipped with the deflector III (2.22) being upwardly directed, and be provided between deflector II (2.21) and deflector III (2.22) greater than etc.
In the gap of the diameter width of half second level tube body (2.2)；
Deflector II (2.21) and deflector III (2.22) are 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 CN106764128A (en) | 2017-05-31 |
| CN106764128B true 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 (5)
| 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 |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9958211B2 (en) * | 2015-03-12 | 2018-05-01 | Bayotech, Inc. | Nested-flow heat exchangers and chemical reactors |
-
2016
- 2016-12-13 CN CN201611146512.4A patent/CN106764128B/en active Active
Patent Citations (5)
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106764128A (en) | 2017-05-31 |
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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. |