CN201413065Y - Chemical heat exchanger - Google Patents
Chemical heat exchanger Download PDFInfo
- Publication number
- CN201413065Y CN201413065Y CN2009200816527U CN200920081652U CN201413065Y CN 201413065 Y CN201413065 Y CN 201413065Y CN 2009200816527 U CN2009200816527 U CN 2009200816527U CN 200920081652 U CN200920081652 U CN 200920081652U CN 201413065 Y CN201413065 Y CN 201413065Y
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- CN
- China
- Prior art keywords
- heat exchanger
- inner core
- chemical industry
- spiral
- urceolus
- 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 - Fee Related
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a chemical heat exchanger. The chemical heat exchanger is characterized in that: the chemical heat exchanger is composed of an inner cylinder (2) and an outer cylinder (4)which are concentric; at least eight spiral connecting sheets (1) are arranged in ring-shaped cavities of the inner cylinder (2) and the outer cylinder (4) in a spaced manner, the inner cylinder (2) and the outer cylinder (4) are connected into a whole by the spiral connecting sheets (1), and at least eight heat exchanging sheets (3) are arranged in the inner cylinder (2). The chemical heat exchanger not only has the advantages of simple as well as reasonable structure, convenient using, high reliability, good economical property and the like, but also effectively increases the heat exchangingefficiency.
Description
Technical field
The utility model relates to chemical industry heat transfer technology field, is specifically related to a kind of chemical industry heat exchanger.
Background technology
Heat exchanger is the device that often can use in the industrial production, and is especially more common in fields such as chemical industry, light industry.Existing heat exchanger is of a great variety, and structural difference is bigger, yet mostly exists shortcomings such as heat exchanger effectiveness is low, complex structure.For example, the inside and outside barrel type heat exchanger of extensive use often has the inner/outer tube heat and transmits difficulty, the little deficiency that waits of heat exchange area.At above-mentioned deficiency of the prior art, this patent has proposed a kind of novel chemical industry heat exchanger.
The utility model content
Technical problem to be solved in the utility model is: how a kind of chemical industry heat exchanger is provided, and this chemical industry has simple and reasonable, heat exchanger effectiveness advantages of higher with heat exchanger, and satisfies easy to use, reliable, economic dispatch requirement.
For achieving the above object, the technical scheme that the utility model adopted is: a kind of chemical industry heat exchanger is provided, it is characterized in that: described chemical industry is made up of concentric inner core and urceolus with heat exchanger; Be arranged at intervals with at least eight spiral braces in the toroidal cavity of described inner core, urceolus, the spiral brace is connected inner core as a whole with urceolus; Be provided with at least eight heat exchanger fins in the described inner core.
According to chemical industry heat exchanger provided by the utility model, it is characterized in that: described spiral brace shape in the shape of a spiral is connected in the outer wall of inner core and the inwall of urceolus.
According to chemical industry heat exchanger provided by the utility model, it is characterized in that: the inwall of described inner core is arranged at intervals with heat exchanger fin along cylinder axis direction, and this heat exchanger fin and inner core are an overall structure.
According to chemical industry heat exchanger provided by the utility model, it is characterized in that: described spiral brace and heat exchanger fin are made by the good Heat Conduction Material of thermal conductivity.
By above-mentioned technical scheme as can be known, chemical industry provided by the utility model heat exchanger structure advantages of simple, the spiral brace good by thermal conductivity connects inner/outer tube, the brace helical design has not only increased heat exchange area, has also guaranteed that the contact-making surface between the different heat exchange mediums is abundant and even simultaneously; The heat exchanger fin of inner core inwall setting has also increased heat exchange area, thereby has improved heat exchanger effectiveness.The utility model is applicable to fields such as chemical industry, light industry, the energy.
Description of drawings
Fig. 1 is the overall structure schematic diagram of chemical industry with heat exchanger;
Fig. 2 is the axial cross section schematic diagram of chemical industry with heat exchanger.
Wherein, 1, spiral brace; 2, inner core; 3, heat exchanger fin; 4, urceolus.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is elaborated.
Fig. 1 is the overall structure schematic diagram of chemical industry provided by the utility model with heat exchanger.Fig. 2 is the axial cross section schematic diagram of chemical industry provided by the utility model with heat exchanger.As shown in the figure, this chemical industry is made up of concentric inner core 2 and urceolus 4 with heat exchanger; Be arranged at intervals with at least eight spiral braces 1 in the toroidal cavity of described inner core 2, urceolus 4, spiral brace 1 is connected as a whole with urceolus 4 inner core 2; Be provided with at least eight heat exchanger fins 3 in the described inner core 2.
Above-mentioned spiral brace 1 shape in the shape of a spiral is connected in the outer wall of inner core 2 and the inwall of urceolus 4.The inwall of above-mentioned inner core 2 is arranged at intervals with heat exchanger fin 3 along cylinder axis direction, and this heat exchanger fin 3 is an overall structure with inner core 2.Above-mentioned spiral brace 1 and heat exchanger fin 3 are made by the good Heat Conduction Material of thermal conductivity.
When this chemical industry uses with heat exchanger, because two kinds of different heat exchange mediums of temperature of reverse feeding in the circular passage between inner core 2 inside and inner core 2, the urceolus 4, and inner core 2, heat exchanger fin 3 and spiral brace 1 are made by the good material of heat conductivility, have so just realized carrying out quickly and efficiently between the different heat exchange medium of inner core 2 inside and outside two kinds of temperature heat transmission.Simultaneously, spiral brace 1 has also been realized the process of heat absorption and release, thereby reaches the purpose that increases heat exchange area and improve heat exchanger effectiveness.In addition, the heat exchanger fin 3 that is provided with in the helical design of spiral brace 1 and the inner core 2 has also increased heat exchange area to greatest extent, has improved heat exchanger effectiveness.
Chemical industry provided by the utility model has simple and reasonable, good reliability, advantage such as easy to use with heat exchanger, is applicable to fields such as chemical industry, light industry, refrigeration.
Though this patent has been made detailed description with above-mentioned preferred embodiment to this patent, be not to limit this patent with the foregoing description.Those skilled in the art should recognize under the situation that does not break away from given technical characterictic of the art of this patent scheme and scope, and the increase that technical characterictic is done, with the replacement of some same contents of this area all should belong to the protection domain of this patent.
Claims (4)
1, a kind of chemical industry heat exchanger is characterized in that: described chemical industry is made up of concentric inner core (2) and urceolus (4) with heat exchanger; Be arranged at intervals with at least eight spiral braces (1) in the toroidal cavity of described inner core (2), urceolus (4), spiral brace (1) is connected as a whole with urceolus (4) inner core (2); Be provided with at least eight heat exchanger fins (3) in the described inner core (2).
2, chemical industry heat exchanger according to claim 1 is characterized in that, described spiral brace (1) shape in the shape of a spiral is connected in the outer wall of inner core (2) and the inwall of urceolus (4).
3, chemical industry heat exchanger according to claim 1 is characterized in that, the inwall of described inner core (2) is arranged at intervals with heat exchanger fin (3) along cylinder axis direction, and this heat exchanger fin (3) is an overall structure with inner core (2).
4, chemical industry heat exchanger according to claim 1 is characterized in that, described spiral brace (1) and heat exchanger fin (3) are made by the good Heat Conduction Material of thermal conductivity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200816527U CN201413065Y (en) | 2009-06-10 | 2009-06-10 | Chemical heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200816527U CN201413065Y (en) | 2009-06-10 | 2009-06-10 | Chemical heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201413065Y true CN201413065Y (en) | 2010-02-24 |
Family
ID=41714948
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200816527U Expired - Fee Related CN201413065Y (en) | 2009-06-10 | 2009-06-10 | Chemical heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201413065Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104515416A (en) * | 2013-09-30 | 2015-04-15 | 香港现代科技有限公司 | Heat exchanger and kit, fluid distribution manifold, turbulator and energy recovery system |
| CN106362608A (en) * | 2016-11-18 | 2017-02-01 | 广西大学 | Cooling mixing tube for chemical engineering |
| CN112629290A (en) * | 2021-01-05 | 2021-04-09 | 东南大学 | Be used for supercritical water screw thread fin double-pipe heat exchanger |
-
2009
- 2009-06-10 CN CN2009200816527U patent/CN201413065Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104515416A (en) * | 2013-09-30 | 2015-04-15 | 香港现代科技有限公司 | Heat exchanger and kit, fluid distribution manifold, turbulator and energy recovery system |
| CN104515416B (en) * | 2013-09-30 | 2019-05-31 | 香港现代科技有限公司 | Heat exchanger and kit, fluid distribution manifold, turbulator and energy recovery system |
| CN110260690A (en) * | 2013-09-30 | 2019-09-20 | 香港现代科技有限公司 | Heat exchanger and external member, fluid distributing manifold, flow spoiler and energy recycling system |
| CN110260690B (en) * | 2013-09-30 | 2021-11-23 | 香港现代科技有限公司 | Heat exchanger and kit, fluid distribution manifold, turbulator and energy recovery system |
| CN106362608A (en) * | 2016-11-18 | 2017-02-01 | 广西大学 | Cooling mixing tube for chemical engineering |
| CN106362608B (en) * | 2016-11-18 | 2019-04-26 | 广西大学 | A kind of cooling mixing pipe for chemical industry |
| CN112629290A (en) * | 2021-01-05 | 2021-04-09 | 东南大学 | Be used for supercritical water screw thread fin double-pipe heat exchanger |
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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: 20100224 Termination date: 20150610 |
|
| EXPY | Termination of patent right or utility model |