CN202002517U - Anti-blocking shell-and-tube heat exchanger with multiple tube bundles - Google Patents
Anti-blocking shell-and-tube heat exchanger with multiple tube bundles Download PDFInfo
- Publication number
- CN202002517U CN202002517U CN2010206615632U CN201020661563U CN202002517U CN 202002517 U CN202002517 U CN 202002517U CN 2010206615632 U CN2010206615632 U CN 2010206615632U CN 201020661563 U CN201020661563 U CN 201020661563U CN 202002517 U CN202002517 U CN 202002517U
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- CN
- China
- Prior art keywords
- tube
- heat exchanger
- shell
- elbow
- bundle
- 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.)
- Expired - Lifetime
Links
- 238000003466 welding Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 claims 1
- 239000012530 fluid Substances 0.000 abstract description 8
- 239000012535 impurity Substances 0.000 abstract description 3
- 230000007774 longterm Effects 0.000 abstract description 3
- 230000008021 deposition Effects 0.000 abstract 1
- 210000002445 nipple Anatomy 0.000 description 6
- 239000003638 chemical reducing agent Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000000452 restraining effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- 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
- F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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
本实用新型公开了一种多管束防堵塞管壳换热器，该换热器包括壳体、管束、短节、变径管、管法兰、180°弯头、管板、换热管和折流板等。通过180°弯头将相邻两管束连接形成通路替代传统换热器的管箱，并实现多管束结构，可消除管箱内的流动死区，避免介质在管箱中产生沉积；提高流体的湍流程度，缩短介质在换热管中的停留时间，防止沉积在换热管内表面的疏松杂质结成牢固的污垢。该新型多管束防堵塞管壳换热器提高了传热效率，保证了换热器的长期稳定运行。
The utility model discloses a multi-tube bundle anti-blocking shell and tube heat exchanger, which includes a shell, a tube bundle, a pup joint, a variable diameter tube, a tube flange, a 180° elbow, a tube plate, a heat exchange tube and Baffles, etc. Two adjacent tube bundles are connected by a 180° elbow to form a passage instead of the tube box of the traditional heat exchanger, and a multi-tube bundle structure can be realized, which can eliminate the flow dead zone in the tube box and avoid the deposition of the medium in the tube box; improve the flow rate of the fluid The degree of turbulence shortens the residence time of the medium in the heat exchange tube and prevents the loose impurities deposited on the inner surface of the heat exchange tube from forming firm dirt. The novel multi-bundle anti-clogging shell-and-tube heat exchanger improves heat transfer efficiency and ensures long-term stable operation of the heat exchanger.
Description
Technical field
The utility model relates to a kind of multitubular bundles anti-clogging shell-and-tube heat exchanger, is applicable on the heat-exchanger rig in fields such as chemical industry, light industry, food, and being particularly useful for tube side fluid is the occasion that contains solid particle, easy fouling or gluey easily stifled medium.
Background technology
All there is certain flow dead in the bobbin carriage of conventional shell-and-tube heat exchanger, when tube side fluid is easily blocked up medium for containing solid particle, easy fouling or glue, because the effect of gravitational settling, adhesion etc., impurity in the medium will slowly deposit in heat exchanger tube and in the dead band of bobbin carriage, on the one hand, the heat exchanger circulation area is reduced, dirtiness resistance increases, the heat-transfer effect variation has increased the energy consumption of whole device; On the other hand, the workload of cleaning heat exchanger increases, and overhaul of the equipments becomes frequently, also can cause the obstruction of whole heat exchanger when serious, directly has influence on the safe and stable operation of device.
Summary of the invention
The shortcoming that the purpose of this utility model is to overcome prior art provides a kind of multitubular bundles anti-clogging shell-and-tube heat exchanger with not enough.
The purpose of this utility model is achieved through the following technical solutions:
A kind of multitubular bundles anti-clogging shell-and-tube heat exchanger comprises housing, tube bank, pipe nipple, reducer pipe, pipe flange, 180 ° of elbows, tube sheet, heat exchanger tube and deflection plates.
180 ° of elbows are connected to form path with two adjacent tube banks, substitute the bobbin carriage of traditional heat exchangers, realize the multitubular bundles structure, eliminate the flow dead in the bobbin carriage, avoid medium to deposit in bobbin carriage; Improve the turbulent extent of medium, shorten the time of staying of medium in heat exchanger tube, prevent that the loose impurity that is deposited on the heat exchanger tube inner surface from forming firm dirt; Improve the heat transfer efficiency of heat exchanger, guaranteed the long-term stability operation of equipment.
Heat exchanger tube is fixed on the tube sheet, and heat exchanger tube is made of some tube banks.Adjacent two tube banks connect into path by 180 ° of elbows.The effect of tube bank is to make minor diameter heat exchanger tube energy and major diameter elbow form path, avoids using the major diameter heat exchanger tube with heat transfer coefficient that reduces heat exchanger and the volume that increases equipment.
Two adjacent tube banks are fixed on the tube sheet with pipe nipple, and fixing mode can be used welding, flange connection etc., preferably uses welding, and welding can reduce distance between restraining with the saving space.Pipe nipple is connected with 180 ° of elbows with pipe flange successively by reducer pipe, has constituted a path.
In the junction of tube bank and elbow, adopt the reducer pipe transition, dwindle elbow diameter, further improve flow velocity, shorten the time of staying of medium in the elbow.Shell side is provided with some deflection plates to increase the turbulent extent of fluid, improves the heat transfer coefficient of fluid.By above measure, can improve the turbulent extent of fluid, eliminate the dead band in bobbin carriage and the heat exchanger tube, guarantee the long-term stability operation of heat exchanger.
Description of drawings
Fig. 1 is the Facad structure schematic diagram of multitubular bundles anti-clogging shell-and-tube heat exchanger; Wherein, 1-housing; The 2-tube bank; The 3-pipe nipple; The 4-reducer pipe; The 5-pipe flange; 6-180 ° of elbow; The 7-tube sheet; The 8-heat exchanger tube; The 9-deflection plate.
Fig. 2 is the right view of multitubular bundles anti-clogging shell-and-tube heat exchanger; Wherein, 5-pipe flange; 6-180 ° of elbow; The 7-tube sheet.
The specific embodiment
Below in conjunction with embodiment and accompanying drawing the utility model is described in further detail, but embodiment of the present utility model is not limited thereto.
Embodiment
Multitubular bundles anti-clogging shell-and-tube heat exchanger is based on traditional shell-and-tube heat exchanger.As shown in Figure 1, housing 1 and deflection plate 9 are structurally basic identical with traditional shell-and-tube heat exchanger, and tube sheet 7 adopts thin tubesheet to be welded in the cylindrical shell.In the tube side heat exchanger tube is divided into some tube banks 2.Arranging by the pattern of equilateral triangle between heat exchanger tube in the tube bank, tube bank and the tube bank is fixed on the tube sheet 7, and the distance of tube bank and tube bank should be as far as possible little, with the compactedness of increase equipment.
Two adjacent tube banks are welded on the tube sheet 7 with pipe nipple 3.Pipe nipple 3 is connected with 180 ° of elbows 6 with pipe flange 5 successively by reducer pipe 4, and two adjacent tube banks constitute a path.As shown in Figure 2, be connected in a manner described with another tube bank, form second path, by that analogy at an end of restraining.
Cleaner fluid enters from shell side, forms turbulent flow under the effect of deflection plate, with the abundant heat exchange of tube side fluid.Contain solid particle, easy fouling or gluey easily stifled medium and enter tube bank, flow through elbow at the terminal reducing of tube bank and enter next one tube bank, finally discharge from the tube side outlet from tube side.When needs clean tube side, take the flushing of flange 5 usefulness clear water apart and get final product.
The foregoing description is the utility model preferred implementation; but embodiment of the present utility model is not restricted to the described embodiments; other any do not deviate from change, the modification done under spiritual essence of the present utility model and the principle, substitutes, combination, simplify; all should be the substitute mode of equivalence, be included within the protection domain of the present utility model.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206615632U CN202002517U (en) | 2010-12-15 | 2010-12-15 | Anti-blocking shell-and-tube heat exchanger with multiple tube bundles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206615632U CN202002517U (en) | 2010-12-15 | 2010-12-15 | Anti-blocking shell-and-tube heat exchanger with multiple tube bundles |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202002517U true CN202002517U (en) | 2011-10-05 |
Family
ID=44705254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206615632U Expired - Lifetime CN202002517U (en) | 2010-12-15 | 2010-12-15 | Anti-blocking shell-and-tube heat exchanger with multiple tube bundles |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202002517U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104165534A (en) * | 2014-08-25 | 2014-11-26 | 哈尔滨工程大学 | Tubular heat exchanger with twisted strips in relaxation fit with protruding tubes |
| CN109405598A (en) * | 2018-11-08 | 2019-03-01 | 上海慧得节能科技有限公司 | Variable diameter tube side heat exchanger for hot-blast stove |
| CN110793351A (en) * | 2019-11-21 | 2020-02-14 | 上海蓝滨石化设备有限责任公司 | A horizontal multi-tube bundle heavy oil heat exchanger |
| CN112146471A (en) * | 2020-09-29 | 2020-12-29 | 扬中申扬换热设备有限公司 | Square shell-and-tube heat exchanger |
-
2010
- 2010-12-15 CN CN2010206615632U patent/CN202002517U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104165534A (en) * | 2014-08-25 | 2014-11-26 | 哈尔滨工程大学 | Tubular heat exchanger with twisted strips in relaxation fit with protruding tubes |
| CN104165534B (en) * | 2014-08-25 | 2017-02-08 | 哈尔滨工程大学 | Tubular heat exchanger with twisted strips in relaxation fit with protruding tubes |
| CN109405598A (en) * | 2018-11-08 | 2019-03-01 | 上海慧得节能科技有限公司 | Variable diameter tube side heat exchanger for hot-blast stove |
| CN109405598B (en) * | 2018-11-08 | 2024-05-14 | 上海慧得节能科技有限公司 | Reducing pipe-line hot-blast stove heat exchanger |
| CN110793351A (en) * | 2019-11-21 | 2020-02-14 | 上海蓝滨石化设备有限责任公司 | A horizontal multi-tube bundle heavy oil heat exchanger |
| CN112146471A (en) * | 2020-09-29 | 2020-12-29 | 扬中申扬换热设备有限公司 | Square shell-and-tube heat exchanger |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20111005 |
|
| CX01 | Expiry of patent term |