CN202902945U - Anticorrosion tube-and-shell type heat exchanger - Google Patents
Anticorrosion tube-and-shell type heat exchanger Download PDFInfo
- Publication number
- CN202902945U CN202902945U CN 201220543144 CN201220543144U CN202902945U CN 202902945 U CN202902945 U CN 202902945U CN 201220543144 CN201220543144 CN 201220543144 CN 201220543144 U CN201220543144 U CN 201220543144U CN 202902945 U CN202902945 U CN 202902945U
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- tube
- heat exchanger
- fixed
- heat exchange
- shell type
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Abstract
Provided is an anticorrosion tube-and-shell type heat exchanger. A heat exchange tube which is coaxial with a shell body is fixed between two fixed tube plates, and a tube-pass split-ranging partition board and the fixed tube plates are arranged on the inner wall of the shell body. The anticorrosion tube-and-shell type heat exchanger is characterized in that a circuit passage is formed by the tube-pass split-ranging partition board and the fixed tube plates through tube-pass liquid and an insulation tube is arranged on the joint of the outer wall of the heat exchange tube and the fixed tube plates. A sacrificial anode tube-pass split-ranging partition board is taken as an anode, metal atoms are electrolyzed to metal ions in the tube-pass liquid to supply electrons for the heat exchange tube, so that the corrosion process that atoms change to ions in the pipeline of the heat exchange tube is retarded or eliminated, the corrosion of the inner wall of the heat exchange tube is avoided, and thus the purpose of heat exchange tube protection is achieved. Meantime the anticorrosion tube-and-shell type heat exchanger is reasonable in design, simple in structure, long in service life, low in product cost, and can be popularized and used in all kinds of tube-and-shell type heat exchangers.
Description
Technical field
The utility model relates to heat exchanger, particularly a kind of can etch-proof shell-and-tube heat exchanger.
Background technology
In industrial production, for realizing a kind equipment of heat transfer process between the material, be referred to as heat exchanger.It is a kind of common apparatus of chemical industry, oil refining, power, the energy, atomic energy and other many industrial department extensive uses.For industry such as the chemical industry that develops rapidly, oil refining, heat exchanger is particularly important.Usually in the construction in chemical plant, heat exchanger accounts for 10~20% of gross investment.In oil plant, heat exchanger accounts for 35~40% of whole technological equipment investment.
In heat transmission equipment, most widely used is shell-and-tube heat exchanger.It is wide that it has selection range, the heat exchange surface easy to clean, and strong adaptability, treating capacity is large, can bear the characteristics such as high temperature and high pressure.To such an extent as to heat exchanger is the achievement that combines the each side such as thermal conduction study, applied mechanics, material science, metallurgical technology, manufacturing technology technical physics.Simultaneously, because the anxiety of the energy has been alleviated in the development of heat exchanger technology greatly.
Carrying out shell-and-tube heat exchanger when design, the material of the various parts and components of heat exchanger should be chosen according to the corrosive nature of the operating pressure of equipment, operating temperature, fluid and to the requirement of the manufacturing process performance of material etc.General operating pressure and operating temperature in order to satisfy equipment both considered from intensity or the rigidity of equipment, was the comparison easy to reach, but to the decay resistance of material, sometimes often became the problem of a complexity.As inconsiderate in this respect, selection is improper, not only can affect the life-span of heat exchanger, and greatly improves the cost of equipment.General heat exchanger mainly is that the temperature by different medium in tube side and the shell side realizes conducting heat.In the oil refining process, because the oil of refining contains H
2S, CO
2Deng corrosive gas, owing to the reasons such as burn into shock and vibration, stress can cause damage by heat exchanger, mainly occur on the heat exchanger tube, because of reasons such as corrosion and scalings, heat exchanger tube is extracted relatively difficulty out, and it is larger to change work difficulty, and tube-to-tube sheet connection mainly adopts Type of Welding to realize, in case replace tubes will affect normal production.In recent years, various countries have also obtained comparatively significant achievement in the research in heat exchanger anticorrosion field and design aspect, and such as the application of novel anticorrosion corrosion material, but new material involves great expense, and the popularization that shortcoming has restricted the heat exchanger aseptic technic such as are not easy to change.
Summary of the invention
In order to overcome the easy fouling of shell-and-tube heat exchanger and the hurtful problem of corrosion heat exchanging organ pipe in the prior art, the purpose of this utility model is to provide a kind of anti-corrosion pipe shell heat exchanger, has characteristics simple in structure, that effect is remarkable, convenient and practical.
In order to achieve the above object, the technical solution of the utility model is achieved in that
A kind of anti-corrosion pipe shell heat exchanger, comprise the Tube Sheet of Heat Exchanger 5 coaxial with housing, be provided with tube pass partition 1 and fixed tube sheet 3 in inner walls, tube pass partition 1 adopts conductive material, form circuit pathways by tube side liquid between tube pass partition 1 and the fixed tube sheet 3, the outer wall of Tube Sheet of Heat Exchanger 5 and fixed tube sheet 3 junctions are provided with insulation tube 8.
Described tube pass partition 1 adopts conductive material, is zinc or magnalium or magnalium Zinc material.
Described insulation tube 8 is the composite steel wire rubber sleeve.
The utility model is by adopting tube pass partition conductive material zinc or magnalium or magnalium Zinc material, zinc or magnalium, magnalium zinc are as anode, form circuit pathways with fixed tube sheet, anode is electrolyzed to produce metal ion by the anode metal atom in tube side liquid, for heat exchanger tube provides electronics, the corrosion process that makes the heat exchanger tube interior conduit be become ion by atom is slowed down or is eliminated, and has avoided the corrosion of heat exchanger tube inwall, has realized the purpose of protection heat exchanger tube; The utility model design protection scope is wide simultaneously; protect effective; and be easy on the structure realize; do not change other function of shell-and-tube heat exchanger; and can directly at labour Tube Sheet of Heat Exchanger checking maintenance the time, implement, can regularly replace, have the advantages such as reasonable in design, that antiseptic property good, product cost is low; prolonged the service life of heat exchanger, can in various shell-and-tube heat exchangers, promote the use of.
Description of drawings
Fig. 1 is the cutaway view of the utility model embodiment 1.
Fig. 2 is partial enlarged drawing among Fig. 1.
Fig. 3 is the electrochemical protection loop schematic diagram that tube pass partition 1 of the present utility model and fixed tube sheet 3 form.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further specified, but the utility model is not limited only to following embodiment.
With reference to Fig. 1, Fig. 2, shell-and-tube heat exchanger, be provided with tube side liquid-inlet 2 and tube side liquid outlet 7 and shell side liquid-inlet 4 and shell side liquid outlet 6 at housing, be provided with tube pass partition 1 in the housing, in housing, be provided with two fixed tube sheets 3, be fixed with the Tube Sheet of Heat Exchanger 5 coaxial with housing between two fixed tube sheets 3, form circuit pathways by tube side liquid between tube pass partition 1 and the fixed tube sheet 3, the outer wall of Tube Sheet of Heat Exchanger 5 and fixed tube sheet 3 junctions are provided with insulation tube 8.
Described pass partition 1 adopts conductive material, is zinc or magnalium or magnalium Zinc material.
Described insulation tube 8 is the composite steel wire rubber sleeve.
Operation principle of the present utility model is: referring to Fig. 3; during use; by tube side liquid-inlet 2 at the heat exchanger shell inwall; fill fluid in the cavity between fixed tube sheet 3 and the tube pass partition 1; consist of tube side fluid; sacrificial anode tube pass partition 1 is immersed in the tube side fluid; as anode; in tube side fluid, be electrolyzed to produce metal ion by metallic atom; metal ion is by fixed tube sheet 3 forming circuit paths; with conducting solution be the electrochemical protection loop that tube side fluid consists of sacrificial anode; the electronics that the anode ionization produces flows to Tube Sheet of Heat Exchanger 5 by the loop; for Tube Sheet of Heat Exchanger 5 provides electronics; changed the current potential of Tube Sheet of Heat Exchanger 5, the corrosion process that makes Tube Sheet of Heat Exchanger 5 be become ion by atom is slowed down or is eliminated, and has avoided the corrosion of Tube Sheet of Heat Exchanger 5 inwalls.
Claims (2)
1. anti-corrosion pipe shell heat exchanger, between two fixed tube sheets (3), be fixed with the Tube Sheet of Heat Exchanger coaxial with housing (5), be provided with tube pass partition 1 in inner walls, also be provided with fixed tube sheet 3, it is characterized in that, tube pass partition (1) forms circuit pathways with fixed tube sheet (3) by tube side liquid, and the outer wall of Tube Sheet of Heat Exchanger (5) and fixed tube sheet (3) junction are provided with insulation tube (8).
2. shell-and-tube heat exchanger according to claim 1 is characterized in that, described insulation tube (8) is the composite steel wire rubber sleeve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220543144 CN202902945U (en) | 2012-10-22 | 2012-10-22 | Anticorrosion tube-and-shell type heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220543144 CN202902945U (en) | 2012-10-22 | 2012-10-22 | Anticorrosion tube-and-shell type heat exchanger |
Publications (1)
Publication Number | Publication Date |
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CN202902945U true CN202902945U (en) | 2013-04-24 |
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ID=48123605
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201220543144 Expired - Fee Related CN202902945U (en) | 2012-10-22 | 2012-10-22 | Anticorrosion tube-and-shell type heat exchanger |
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CN (1) | CN202902945U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106835149A (en) * | 2017-01-09 | 2017-06-13 | 青岛双瑞海洋环境工程股份有限公司 | A kind of heat exchanger tube outer wall galvanic anode protection protecting system |
CN114392707A (en) * | 2022-02-25 | 2022-04-26 | 山东大明精细化工有限公司 | Reactor heat exchange system for producing sulfonic acid surfactant |
-
2012
- 2012-10-22 CN CN 201220543144 patent/CN202902945U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106835149A (en) * | 2017-01-09 | 2017-06-13 | 青岛双瑞海洋环境工程股份有限公司 | A kind of heat exchanger tube outer wall galvanic anode protection protecting system |
CN106835149B (en) * | 2017-01-09 | 2019-03-05 | 青岛双瑞海洋环境工程股份有限公司 | A kind of heat exchanger tube outer wall galvanic anode protection protecting system |
CN114392707A (en) * | 2022-02-25 | 2022-04-26 | 山东大明精细化工有限公司 | Reactor heat exchange system for producing sulfonic acid surfactant |
CN114392707B (en) * | 2022-02-25 | 2023-09-22 | 山东大明精细化工有限公司 | Reactor heat exchange system for producing sulfonic acid surfactant |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130424 Termination date: 20141022 |
|
EXPY | Termination of patent right or utility model |