CN104457385B - One kind tube bank self-support heat exchanger - Google Patents
One kind tube bank self-support heat exchanger Download PDFInfo
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- CN104457385B CN104457385B CN201410669845.XA CN201410669845A CN104457385B CN 104457385 B CN104457385 B CN 104457385B CN 201410669845 A CN201410669845 A CN 201410669845A CN 104457385 B CN104457385 B CN 104457385B
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Abstract
The heat-exchanging tube bundle in collar aperture plate supporting type heat exchanger, including pipe heat exchanger, the pipe heat exchanger is restrained the present invention relates to one kind to support mutually by the fixed sleeving being sleeved on outside single heat exchange tube, heat-exchanging tube bundle circumferentially passes through support plate supporting and fixing.Closely connected between fixed sleeving press flute and heat exchanger tube.Compared with prior art, the beneficial effects of the invention are as follows：1) medium in shell side forms continuous, the uniform flow path of complexity between heat exchanger tube, improves its turbulent extent, is thinned the boundary layer of flowing, reduces heat transmission resistance, so as to improve heat exchange efficiency；2) equipment volume is small, and manufacturing cost is low；3) no baffle plate in shell side, eliminates the flow dead in shell side, reduces the pressure drop of shell side medium：4) non-blind area in shell side, less scaling；Flow velocity is higher in shell side, reduces the accumulation of impurity in medium：5) large area through hole is opened up on orifice plate, compared to traditional deflection plate, heat exchanger tube is installed and dismantled very convenient.
Description
Technical field
The present invention relates to a kind of pipe heat exchanger, more particularly to a kind of tube bank sleeve pipe for media for heat exchange in coking industry
Orifice plate supporting type heat exchanger, can effectively solve the problem that impurity accumulation sedimentation, the problems such as heat exchange efficiency is low, shell side resistance is big.
Background technology
Tubular type (also known as shell-and-tube, shell and tube) heat exchanger is most typical dividing wall type heat exchanger, its application industrially
There is long history, and still occupy leading position in all heat exchangers so far.Pipe heat exchanger is main by housing, pipe
How rounded beam, tube sheet and envelope first class sections composition, housing is, and inside is equipped with bundle of parallel tubes, and tube bank two ends are fixed on tube sheet.
The two kinds of fluids exchanged heat in pipe heat exchanger, one kind is in Bottomhole pressure, and its stroke is referred to as tube side；One kind exists
Pipe is outer to be flowed, and its stroke is referred to as shell side, and the wall of tube bank is heat-transfer area.To improve extratubal fluid heat transfer coefficient, generally in shell
A number of horizontal baffle plate is installed in vivo, baffle plate can not only prevent fluid short, increase fluid velocity, also force
Fluid, by tube bank, greatly increases less turbulence by the regulation multiple cross-flow in path.Conventional plate washer has discount vibram outlet shape and full-circle spray pattern
Two kinds.Fluid is often once referred to as a tube side in pipe by tube bank, is often once referred to as a shell side by housing.To improve pipe
The speed of interior fluid, sets dividing plate by whole pipe equipartitions into some groups in the end socket of two ends.So, fluid can every time only
Tube bank is come and gone by partial tube multiple, referred to as multitube distance.Equally, to improve the outer flow velocity of pipe, longitudinal direction can be installed in housing
Plate washer makes fluid multipass shell space, claims muitishell.
It is low generally to there is heat exchange efficiency in traditional shell-and-tube heat exchanger, the accumulation of shell side medium impurity, hardly possible cleaning, complicated etc.
Shortcoming.As shell side supporting tends to simplify, in recent years, occur in that shell side does not need support i.e. tube side self-supporting structure.Mesh
Before, it is known that tube bank self-supporting form have punching membrane chip, distorted elliptical tubular type, variable cross-section tubular type etc., but generally existing makes
The problem of processing difficulties, non-easy cleaning, detachable maintaining are inconvenient.
The content of the invention
The invention provides a kind of new tube bank self-support heat exchanger, support plate and heat exchange are realized using fixed sleeving
Support and connection between pipe, effectively improve heat exchange efficiency, reduce shell side accumulation impurity, additionally with quick detachable, maintenance and
Cleaning, the advantages of equipment takes up an area small, low cost.
In order to achieve the above object, the present invention is realized using following technical scheme：
Heat-exchanging tube bundle in one kind tube bank self-support heat exchanger, including pipe heat exchanger, the pipe heat exchanger passes through
The fixed sleeving being sleeved on outside single heat exchange tube is supported mutually, and heat-exchanging tube bundle circumferentially passes through support plate supporting and fixing.
The fixed sleeving length is 1~1.5 times of heat exchanger tube node length, fixed sleeving compacting and heat exchange tube shape phase
The groove of adaptation realizes the close connection between heat exchanger tube.
The pipe heat exchanger is in floating head type pipe heat exchanger, U-shaped pipe heat exchanger or fixed tube-sheet exchanger
Any, its tube side is single tube journey or multitube distance.
The support plate is that the through hole being adapted with heat-exchanging tube bundle exterior contour is opened up on full-circle spray pattern support plate, support plate,
And perforated area is determined according to single tube journey or multitube distance.
The heat exchanger tube is any of transversally flute tube, thread groove tube, helix tube, bellows, shaped telescopic tube or finned tube.
Compared with prior art, the beneficial effects of the invention are as follows：
1) medium in shell side forms continuous, the uniform flow path of complexity between heat exchanger tube, improves its turbulent extent, subtracts
The boundary layer of thin flowing, reduces heat transmission resistance, so as to improve heat exchange efficiency；
2) due to the raising of heat exchange efficiency, heat exchange area can be reduced, equipment volume declines therewith, in addition the heat exchanger without
Deflection plate so that its manufacturing cost is substantially reduced；
3) due to no baffle plate in shell side, heat exchanger tube is mutually supported by fixed sleeving, shell-side fluid from fixed sleeving it
Between gap pass through, it is thus eliminated that the flow dead in shell side, reduces the pressure drop of shell side medium：
4) due to non-blind area in shell side, therefore, the heat exchanger is less scaling；In addition, the special supporting construction of this heat exchanger
Higher flow velocity can be formed in shell side, so as to also reduce the accumulation of impurity in medium：
5) large area through hole is opened up on orifice plate, compared to traditional deflection plate, heat exchanger tube is installed and dismantled very convenient.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention.
Fig. 2 is support plate and heat-exchanging tube bundle connection diagram.
In figure：1. 5. fixed tube sheet of bobbin carriage 2. tube side material inlet, 3. tube side material outlet, 4. channel flange 6.
The shell flange of 11. saddle of body flange 7. shell-side cylinder, 8. shell side material outlet, 9. shell side material inlet, 10. heat exchanger tube 12.
13. the Floating Head Flange 19. of 17. hook circle of outer 16. pass partition of skull of the outer skull flange 15. of floating tubesheet 14. 18. is raised the nose above water to breathe
20. the support plate of fixed sleeving 21.
Embodiment
The embodiment to the present invention is described further below in conjunction with the accompanying drawings：
See Fig. 1, be the structural representation of the present invention, a kind of tube bank self-support heat exchanger of the present invention, including pipe type heat transfer
Heat-exchanging tube bundle in device, the pipe heat exchanger is supported mutually by the fixed sleeving 20 being sleeved on outside single heat exchange tube 10, is changed
Heat pipe bundle circumferentially passes through the supporting and fixing of support plate 21.
The length of fixed sleeving 20 is 1~1.5 times of the node length of heat exchanger tube 10, and fixed sleeving 20 is suppressed and heat exchanger tube
The adaptable groove of 10 shapes realizes the close connection between heat exchanger tube 10.
The pipe heat exchanger is in floating head type pipe heat exchanger, U-shaped pipe heat exchanger or fixed tube-sheet exchanger
Any, its tube side is single tube journey or multitube distance.
The support plate 21 is to be opened up on full-circle spray pattern support plate, support plate 21 and leading to that heat-exchanging tube bundle exterior contour is adapted
Hole, and perforated area is determined according to single tube journey or multitube distance.
The heat exchanger tube 10 is any in transversally flute tube, thread groove tube, helix tube, bellows, shaped telescopic tube or finned tube
Kind.
Below by taking floating head type pipe heat exchanger as an example to the present invention it is a kind of restrain self-support heat exchanger overall structure and
Operation principle is described as follows：
As shown in figure 1, bobbin carriage 1 is connected with channel flange 4, tube side is divided into multi-way (root provided with pass partition 16 in bobbin carriage 1
Number of passes is determined according to concrete condition), tube side material inlet 2, tube side material outlet 3 are respectively provided at front-end pipe box about 1 both sides.Shell side
Cylinder 7 is connected with shell flange 6, shell flange 12, and the lower section of shell-side cylinder 7 is provided with saddle 11, shell side material outlet 8, shell side thing
Material entrance 9 is respectively provided at the both sides of shell-side cylinder 7.Fixed tube sheet 5 is placed between channel flange 4 and shell flange 6, floating tubesheet 13
It is placed between hook circle 17, Floating Head Flange 18.Floating Head Flange 18 and floating head 19, outer skull 15 is connected with outer skull flange flange 14.
Heat-exchanging tube bundle is fixed between fixed tube sheet 5 and Floating Head Flange 18, spaced apart, right on every heat exchanger tube 10
Answer and fixed sleeving 20 is provided with support plate 21, the length of fixed sleeving 20 is not less than the length of 10 1 node of heat exchanger tube, fixed cover
It is coincide after pipe 20 is repressed with heat exchange tube shape, the close connection of formation between the two acts on support plate 21, realizes tube bank certainly
Supporting.Shell-side fluid flows through from the gap between fixed sleeving 20, forms complicated continuous, uniform runner, effective to improve
Heat exchange efficiency.Tube side medium is entered by tube side material inlet 2, is left by tube side material outlet 3.Shell side medium is by medium inlet
9 enter, and are left by media outlet 8.
See Fig. 2, be support plate 21 and heat-exchanging tube bundle connection diagram.Support plate 21 uses full-circle spray pattern orifice plate, according to heat exchange
The arrangement form of tube bank opens up large area through hole, and the exterior contour of its through hole and the overall outline of heat-exchanging tube bundle are adapted, single
10 sets of root heating tube is loaded onto and heat-exchanging tube bundle is formed after fixed sleeving 20, and heat-exchanging tube bundle is integrally passed through from the through hole of support plate 21, Gu
Determine close contact between sleeve pipe 20, mutually supporting, form self-supporting formula heat-exchanging tube bundle structure.
Claims (1)
1. one kind tube bank self-support heat exchanger, including pipe heat exchanger, it is characterised in that the heat exchange in the pipe heat exchanger
Tube bank is supported mutually by the fixed sleeving being sleeved on outside single heat exchange tube, and heat-exchanging tube bundle circumferentially passes through support plate supporting and fixing；
The fixed sleeving length is 1~1.5 times of heat exchanger tube node length, adaptable recessed of fixed sleeving compacting and heat exchange tube shape
Groove realizes the close connection between heat exchanger tube；The support plate is to be opened up and heat-exchanging tube bundle on full-circle spray pattern support plate, support plate
The adaptable through hole of exterior contour, and perforated area is determined according to single tube journey or multitube distance；
The pipe heat exchanger is floating head type pipe heat exchanger, and bobbin carriage is connected with channel flange, will provided with pass partition in bobbin carriage
Tube side is divided into multi-way, and tube side material inlet, tube side material outlet are respectively provided at both sides above and below front-end pipe box；Shell-side cylinder and cylinder
Flange is connected, and saddle is provided with below shell-side cylinder, shell side material outlet, shell side material inlet are respectively provided at shell-side cylinder both sides；
Fixed tube sheet is placed between channel flange and shell flange, and floating tubesheet is placed between hook circle, Floating Head Flange；Floating Head Flange is with floating
Head, outer skull is connected with outer skull flange；
Heat-exchanging tube bundle is fixed between fixed tube sheet and Floating Head Flange, spaced apart on every heat exchanger tube, correspondence support plate
Place is provided with fixed sleeving, is coincide after fixed sleeving is repressed with heat exchange tube shape, forms close connection between the two, acts on branch
Hold on plate, realize tube bank self-supporting；Shell-side fluid flows through from the gap between fixed sleeving, forms complicated continuous, uniform
Runner, effectively raises heat exchange efficiency；Tube side medium is entered by tube side material inlet, is left by tube side material outlet；Shell side
Medium is entered by shell side material inlet, is left by shell side material outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410669845.XA CN104457385B (en) | 2014-11-21 | 2014-11-21 | One kind tube bank self-support heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410669845.XA CN104457385B (en) | 2014-11-21 | 2014-11-21 | One kind tube bank self-support heat exchanger |
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| Publication Number | Publication Date |
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| CN104457385A CN104457385A (en) | 2015-03-25 |
| CN104457385B true CN104457385B (en) | 2017-07-28 |
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| CN201410669845.XA Active CN104457385B (en) | 2014-11-21 | 2014-11-21 | One kind tube bank self-support heat exchanger |
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Families Citing this family (3)
| 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 |
| CN108500577A (en) * | 2017-12-07 | 2018-09-07 | 浙江星卓换热设备有限公司 | A kind of processing technology of the bobbin carriage with end socket |
| CN109556431A (en) * | 2018-11-23 | 2019-04-02 | 上海慧得节能科技有限公司 | Normalized assembled heat exchanger |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103063056A (en) * | 2012-12-28 | 2013-04-24 | 朱冬生 | Pipe casing type heat exchanger |
| CN203758345U (en) * | 2014-01-22 | 2014-08-06 | 珠海格力电器股份有限公司 | Shell and tube exchanger supporting structure and shell and tube exchanger |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5653284A (en) * | 1995-11-21 | 1997-08-05 | Hudson Products Corporation | Heat pipe heat exchanger tubesheet |
| CN2596308Y (en) * | 2003-01-17 | 2003-12-31 | 田雅杰 | Wave node (or corrugate) heat exchanging tube with protective sleeve |
| CN103376018B (en) * | 2012-04-20 | 2015-09-02 | 约克（无锡）空调冷冻设备有限公司 | A kind of tube bank supporting member for shell-and-tube heat exchanger |
| CN203501884U (en) * | 2013-07-03 | 2014-03-26 | 自贡鑫泰机电设备有限公司 | Protective structure of finned tube of air cooler |
| CN204268950U (en) * | 2014-11-21 | 2015-04-15 | 中冶焦耐工程技术有限公司 | A kind of tube bank self-support heat exchanger |
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2014
- 2014-11-21 CN CN201410669845.XA patent/CN104457385B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103063056A (en) * | 2012-12-28 | 2013-04-24 | 朱冬生 | Pipe casing type heat exchanger |
| CN203758345U (en) * | 2014-01-22 | 2014-08-06 | 珠海格力电器股份有限公司 | Shell and tube exchanger supporting structure and shell and tube exchanger |
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| Publication number | Publication date |
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| CN104457385A (en) | 2015-03-25 |
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Effective date of registration: 20180726 Address after: 116085 128 high energy street, Qixian Ling high tech Industrial Park, Dalian, Liaoning Patentee after: ACRE Coking And Refractory (Dalian) Engineering Consulting Corp., MCC Address before: 116085 128 high energy street, Qixian Ling high tech Industrial Park, Dalian, Liaoning Patentee before: ACRE Coking and Refractory Engineering Consulting Corporation, MCC |