CN106197120A - A kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element - Google Patents
A kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element Download PDFInfo
- Publication number
- CN106197120A CN106197120A CN201610748572.7A CN201610748572A CN106197120A CN 106197120 A CN106197120 A CN 106197120A CN 201610748572 A CN201610748572 A CN 201610748572A CN 106197120 A CN106197120 A CN 106197120A
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- China
- Prior art keywords
- petal
- heat exchanger
- full
- orifice plate
- spray pattern
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Classifications
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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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/24—Arrangements for promoting turbulent flow of heat-exchange media, e.g. by plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2210/00—Heat exchange conduits
- F28F2210/08—Assemblies of conduits having different features
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- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention relates to a kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element, including multiple full-circle spray pattern orifice plates along the parallel longitudinal setting of heat exchanger, and multiple pass perpendicularly through the petal heat exchanger tube that full-circle spray pattern orifice plate is connected with two ends tube sheet；Described petal heat exchanger tube uses that plain tube is integrally formed makes, and its two ends and tube sheet junction are straight length, and middle part is pressed into petal pipeline section, and petal pipeline section is along longitudinally having straight groove or spiral slot；The through hole that on full-circle spray pattern orifice plate, corresponding petal pipeline section passes through is manhole, and its diameter matches with petal pipeline section cross section maximum outside diameter.The present invention utilizes the combination of special shape between heat exchanger tube and orifice plate through hole, is effectively improved the heat exchange efficiency of heat exchanger, reduces the generation of dirt, reduce shell side resistance, solve shell-side fluid skewness, the problem of hull vibration, additionally there is convenient disassembly, reduce the advantages such as equipment, cost are low.
Description
Technical field
The present invention relates to technical field of heat exchangers, particularly relate to a kind of petal heat exchanger tube and change with full-circle spray pattern orifice plate combination type
Thermal element.
Background technology
Shell-and-tube heat exchanger is widely used in the fields such as chemical industry, oil, environmental protection, occupies critical role in the industrial production,
Due to its low cost of manufacture, easy to clean, treating capacity is big, and reliable operation, is also to use most heat exchanger-type in actual production
Type.
Straight tube heat exchanger tube is the parts being most frequently with in shell-and-tube heat exchanger, and tubular form is single, itself and segmental baffle
Coordinating cross-flow heat exchange, heat exchange efficiency is the highest, and easily makes deflection plate outer edge area produce bigger flow dead, and dirt deposition is tight
Weight, fluid orthogonal is easily generated shell vibrating after clashing into housing, causes shell side pressure loss bigger.
Summary of the invention
The invention provides a kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element, utilize heat exchanger tube and hole
The combination of special shape between plate through hole, is effectively improved the heat exchange efficiency of heat exchanger, reduces the generation of dirt, reduces shell side resistance,
Solve shell-side fluid skewness, the problem of hull vibration, additionally there is convenient disassembly, to reduce equipment, cost low etc. excellent
Point.
In order to achieve the above object, the present invention realizes by the following technical solutions:
A kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element, set along heat exchanger is parallel longitudinal including multiple
The full-circle spray pattern orifice plate put, and multiple pass perpendicularly through the petal heat exchanger tube that full-circle spray pattern orifice plate is connected with two ends tube sheet；Described petal
Shape heat exchanger tube uses that plain tube is integrally formed makes, and its two ends and tube sheet junction are straight length, and middle part is pressed into petal pipe
Section, petal pipeline section is along longitudinally having straight groove or spiral slot；The through hole that on full-circle spray pattern orifice plate, corresponding petal pipeline section passes through
For manhole, its diameter matches with petal pipeline section cross section maximum outside diameter.
The petal number of described petal pipeline section is 4-6.
Compared with prior art, the invention has the beneficial effects as follows:
1) set petal pipeline section in the middle part of heat exchanger tube, by the body corrugated extruding of circumference, tube side fluid turbulent flow can be improved
Degree, thinning flow boundary layer, reduce heat transmission resistance, improve heat exchange efficiency；
2) petal heat exchanger tube two ends are straight length, are conducive to itself and the fixing of tube sheet and support；
3) due to the particularity of shape, can form the slit flowing of complexity in petal heat exchanger tube, tube side fluid is to pipe
Wall washes away acutely, makes tube wall not be easily formed dirt, it is achieved automatically to clear up；
4) due to the raising of heat exchange efficiency, making heat exchange area reduce, equipment volume declines therewith so that it is manufacturing cost is significantly
Reduce；
5) petal-shaped structure of corresponding heat exchanger tube main body, use full-circle spray pattern orifice plate, it is to avoid fluid directly clashes into housing, fall
The vibration of low heat exchanger, removes dead band, reduces shell-side pressure drop, less scaling in shell side；
6) shell-side fluid flows out from the space jet between full-circle spray pattern orifice plate manhole and petal heat exchanger tube, enhances
The turbulent flow of fluid, makes fluid distrbution more uniform, is conducive to improving the heat transfer effect of heat exchanger.
Accompanying drawing explanation
Fig. 1 is the partial structurtes schematic diagram of petal heat exchanger tube of the present invention.
Fig. 2 is the schematic cross-section at petal heat exchanger tube of the present invention and full-circle spray pattern orifice plate combination.
In figure: 1. the petal heat exchanger tube of straight length 2. petal pipeline section 3. full-circle spray pattern orifice plate 4. manhole 5.
Detailed description of the invention
Below in conjunction with the accompanying drawings the detailed description of the invention of the present invention is described further:
As Figure 1-Figure 2, the petal heat exchanger tube of one of the present invention and full-circle spray pattern orifice plate combination type heat exchange element, bag
Include multiple full-circle spray pattern orifice plate 3 along the parallel longitudinal setting of heat exchanger, and multiple pass perpendicularly through full-circle spray pattern orifice plate 3 and two ends tube sheet phase
Petal heat exchanger tube 5 even；Described petal heat exchanger tube 5 uses that plain tube is integrally formed to be made, its two ends and tube sheet junction
For straight length 1, middle part is pressed into petal pipeline section 2, and petal pipeline section 2 is along longitudinally having straight groove or spiral slot；Full-circle spray pattern
The through hole that on orifice plate 3, corresponding petal pipeline section 2 passes through is manhole 4, its diameter and petal pipeline section 2 cross section maximum outside diameter
Match.
The petal number of described petal pipeline section 2 is 4-6.
A kind of petal heat exchanger tube of the present invention with the operation principle of full-circle spray pattern orifice plate combination type heat exchange element is: heat exchange
Pipe uses smooth straight to make petal-shaped, forms circumference wave structure, and body two ends keep straight tube-like, and tube side fluid is at circumference
Under the extruding of wave structure, form complicated slit flowing and be rapidly achieved turbulent flow, effectively reduce dirt in pipe, strengthen heat transfer；Shell
Cheng Liuti with the form outflow of jet, strengthens the turbulent flow of fluid from the adjacent petal design space of petal type heat exchanger tube, and raising is changed
The heat transfer effect of hot device.
The above, the only present invention preferably detailed description of the invention, but protection scope of the present invention is not limited thereto,
Any those familiar with the art in the technical scope that the invention discloses, according to technical scheme and
Inventive concept equivalent or change in addition, all should contain within protection scope of the present invention.
Claims (2)
1. a petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element, it is characterised in that include multiple along heat exchanger
The full-circle spray pattern orifice plate of parallel longitudinal setting, and multiple pass perpendicularly through the petal heat exchange that full-circle spray pattern orifice plate is connected with two ends tube sheet
Pipe；Described petal heat exchanger tube uses that plain tube is integrally formed makes, and its two ends and tube sheet junction are straight length, and middle part is suppressed
Becoming petal pipeline section, petal pipeline section is along longitudinally having straight groove or spiral slot；Corresponding petal pipeline section on full-circle spray pattern orifice plate
The through hole passed through is manhole, and its diameter matches with petal pipeline section cross section maximum outside diameter.
The petal heat exchanger tube of one the most according to claim 1 and full-circle spray pattern orifice plate combination type heat exchange element, its feature exists
In, the petal number of described petal pipeline section is 4-6.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610748572.7A CN106197120A (en) | 2016-08-29 | 2016-08-29 | A kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610748572.7A CN106197120A (en) | 2016-08-29 | 2016-08-29 | A kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106197120A true CN106197120A (en) | 2016-12-07 |
Family
ID=57527187
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610748572.7A Pending CN106197120A (en) | 2016-08-29 | 2016-08-29 | A kind of petal heat exchanger tube and full-circle spray pattern orifice plate combination type heat exchange element |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106197120A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107255426A (en) * | 2017-08-11 | 2017-10-17 | 中冶焦耐(大连)工程技术有限公司 | The deflection element and its method of work of a kind of shell-and-tube heat exchanger |
| CN107990761A (en) * | 2017-12-14 | 2018-05-04 | 佛山科学技术学院 | A kind of shell-and-tube heat exchanger of full-circle spray pattern orifice-baffle support axial notch heat exchanger tube |
| CN108007255A (en) * | 2017-12-14 | 2018-05-08 | 佛山科学技术学院 | A kind of shell-and-tube heat exchanger of the axial groove heat exchange tube of deflecting fence support |
| US10995998B2 (en) | 2015-07-30 | 2021-05-04 | Senior Uk Limited | Finned coaxial cooler |
| US11029095B2 (en) | 2015-07-30 | 2021-06-08 | Senior Uk Limited | Finned coaxial cooler |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1372122A (en) * | 2001-02-28 | 2002-10-02 | 刘富春 | Pipe material and production method thereof |
| CN2762050Y (en) * | 2004-12-03 | 2006-03-01 | 王正鹏 | Multihead screw heat exchange pipe |
| CN200993547Y (en) * | 2006-12-22 | 2007-12-19 | 卢秉威 | Baffle plate with special hole |
| CN101650138A (en) * | 2009-07-03 | 2010-02-17 | 广州联合冷热设备有限公司 | Shell-and-tube heat exchanger |
| JP2010078233A (en) * | 2008-09-26 | 2010-04-08 | Regal Joint Co Ltd | Shell-and-tube exchanger |
| CN203443416U (en) * | 2013-05-31 | 2014-02-19 | 茂名市茂港电力设备厂有限公司 | Shell and tube heat exchanger |
| CN104848726A (en) * | 2015-06-05 | 2015-08-19 | 杭州沈氏节能科技股份有限公司 | Multi-head spiral section tube and multi-head spirally-fluted heat exchange tube |
| CN105841523A (en) * | 2016-05-31 | 2016-08-10 | 中冶焦耐工程技术有限公司 | Corrugated straight pipe heat exchanger and heat exchange method |
| CN206037803U (en) * | 2016-08-29 | 2017-03-22 | 中冶焦耐(大连)工程技术有限公司 | Petaloid heat exchange tube and whole circular orifice plate combination formula heat transfer component |
-
2016
- 2016-08-29 CN CN201610748572.7A patent/CN106197120A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1372122A (en) * | 2001-02-28 | 2002-10-02 | 刘富春 | Pipe material and production method thereof |
| CN2762050Y (en) * | 2004-12-03 | 2006-03-01 | 王正鹏 | Multihead screw heat exchange pipe |
| CN200993547Y (en) * | 2006-12-22 | 2007-12-19 | 卢秉威 | Baffle plate with special hole |
| JP2010078233A (en) * | 2008-09-26 | 2010-04-08 | Regal Joint Co Ltd | Shell-and-tube exchanger |
| CN101650138A (en) * | 2009-07-03 | 2010-02-17 | 广州联合冷热设备有限公司 | Shell-and-tube heat exchanger |
| CN203443416U (en) * | 2013-05-31 | 2014-02-19 | 茂名市茂港电力设备厂有限公司 | Shell and tube heat exchanger |
| CN104848726A (en) * | 2015-06-05 | 2015-08-19 | 杭州沈氏节能科技股份有限公司 | Multi-head spiral section tube and multi-head spirally-fluted heat exchange tube |
| CN105841523A (en) * | 2016-05-31 | 2016-08-10 | 中冶焦耐工程技术有限公司 | Corrugated straight pipe heat exchanger and heat exchange method |
| CN206037803U (en) * | 2016-08-29 | 2017-03-22 | 中冶焦耐(大连)工程技术有限公司 | Petaloid heat exchange tube and whole circular orifice plate combination formula heat transfer component |
Non-Patent Citations (1)
| Title |
|---|
| 冯骉: "《食品工程原理》", 31 August 2005 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10995998B2 (en) | 2015-07-30 | 2021-05-04 | Senior Uk Limited | Finned coaxial cooler |
| US11029095B2 (en) | 2015-07-30 | 2021-06-08 | Senior Uk Limited | Finned coaxial cooler |
| CN107255426A (en) * | 2017-08-11 | 2017-10-17 | 中冶焦耐(大连)工程技术有限公司 | The deflection element and its method of work of a kind of shell-and-tube heat exchanger |
| CN107990761A (en) * | 2017-12-14 | 2018-05-04 | 佛山科学技术学院 | A kind of shell-and-tube heat exchanger of full-circle spray pattern orifice-baffle support axial notch heat exchanger tube |
| CN108007255A (en) * | 2017-12-14 | 2018-05-08 | 佛山科学技术学院 | A kind of shell-and-tube heat exchanger of the axial groove heat exchange tube of deflecting fence support |
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Legal Events
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|---|---|---|---|
| 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 |
Application publication date: 20161207 |
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| RJ01 | Rejection of invention patent application after publication |