CN208075653U - Chemical industry high-performance heat exchanger - Google Patents
Chemical industry high-performance heat exchanger Download PDFInfo
- Publication number
- CN208075653U CN208075653U CN201820418843.7U CN201820418843U CN208075653U CN 208075653 U CN208075653 U CN 208075653U CN 201820418843 U CN201820418843 U CN 201820418843U CN 208075653 U CN208075653 U CN 208075653U
- Authority
- CN
- China
- Prior art keywords
- heat
- inlet tube
- heat dissipation
- heat exchange
- dissipation tank
- 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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Classifications
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- 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
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of chemical industry high-performance heat exchangers,Including gas inlet tube,Gas outlet,Water inlet tube,Water outlet tube and heat exchange fill,And gas inlet tube,Gas outlet, which penetrates through, is connected to the upper end that heat exchange fills,Water inlet tube,The perforation of water outlet tube is connected to heat exchange and fills on side wall,This heat exchanger apparatus passes through water feed liquor water inlet tube,Water is flowed out by major flow duct and Zhi Liuguan using water outlet tube,Wherein,Hot gas enters gas inlet tube,Heat dissipation tank is ejected into multiple heat-conducting blocks from puff prot,Carry out heat exchange,And,Air-flow drives the flutter up and down under the action of the spring of entire heat dissipation tank,So that the heat of heat dissipation tank can be passed to uniformly and effectively on Zhi Liuguan,Prevent heat build-up,On the other hand,Cylinder thermal vias can take away major flow duct heat,Heat dissipation convex block further expands heat dissipation area,So that the heat exchange efficiency of entire heat exchanger greatly increases.
Description
Technical field
The utility model is related to chemical technology field more particularly to a kind of chemical industry high-performance heat exchangers.
Background technology
In chemical field, heat exchanger is the equipment that the partial heat of hot fluid is passed to cold fluid, also known as heat exchange
Device.Heat exchanger occupies an important position in chemical industry, oil, power, food and other many industrial productions, in Chemical Manufacture
Heat exchanger can be used as heater, cooler, condenser, evaporator and reboiler etc., be widely used；Existing heat exchanger heat exchange effect
Rate is relatively low, and heat exchange is slow, for this purpose, proposing a kind of chemical industry high-performance heat exchanger.
Utility model content
Purpose of the utility model is to solve disadvantages existing in the prior art, and a kind of chemical industry proposed is with efficiently
Heat exchanger.
To achieve the goals above, the utility model uses following technical solution：
A kind of chemical industry high-performance heat exchanger, including gas inlet tube, gas outlet, water inlet tube, water outlet tube and heat exchange fill,
And gas inlet tube, gas outlet penetrate through and are connected to the upper end that heat exchange fills, water inlet tube, the perforation of water outlet tube are connected to heat exchange and fill
On side wall, which is characterized in that the water inlet tube and water outlet tube are mutual by a major flow duct for filling inner cavity positioned at heat exchange
Perforation connection, the heat exchange fill the cylinder thermal vias that casting forms front and back intercommunication；
The both ends of the Zhi Liuguan of a side wall perforation piece circulating reflux of grafting for the major flow duct, and the other side of Zhi Liuguan
Equipped with heat dissipation tank, Zhi Liuguan is wound on the side wall of heat dissipation tank, and the bottom of the heat dissipation tank is connected to what heat exchange filled by spring
Inner cavity lower curtate, and the side wall perforation of heat dissipation tank is connected with multiple puff prots, and the opening spray of puff prot is located at major flow duct side wall
Between the multiple heat-conducting block cracks connected, the inner cavity upper end perforation of the heat dissipation tank is connected with sleeve, and slides and insert in sleeve
It is connected to gas inlet tube.
Preferably, the surface of internal cavity of the cylinder thermal vias is connected with multiple heat dissipation convex blocks.
Preferably, the heat-conducting block and puff prot at least 16, and equidistantly distributed.
Preferably, the bottom that the heat exchange fills is connected with universal wheel.
Preferably, the Zhi Liuguan, which is slided up and down, is wrapped in heat dissipation tank surface.
Compared with prior art, the utility model has the beneficial effects that：This heat exchanger apparatus passes through water feed liquor water inlet tube, water
It is flowed out using water outlet tube by major flow duct and Zhi Liuguan, wherein hot gas enters gas inlet tube, heat dissipation tank from puff prot
Multiple heat-conducting blocks are ejected into, heat exchange is carried out, moreover, air-flow drives the flutter up and down under the action of the spring of entire heat dissipation tank, from
And the heat of heat dissipation tank is uniformly and effectively passed on Zhi Liuguan, heat build-up is prevented, on the other hand, cylinder heat dissipation is logical
Hole can take away major flow duct heat, and heat dissipation convex block further expands heat dissipation area, so that the heat exchange of entire heat exchanger
Efficiency greatly increases.
Description of the drawings
Fig. 1 be the utility model proposes structural schematic diagram.
In figure：Gas inlet tube 1, gas outlet 2, water inlet tube 3, water outlet tube 4, major flow duct 5, cylinder thermal vias 6,
Radiate convex block 7, heat-conducting block 8, Zhi Liuguan 9, heat dissipation tank 10, spring 11, sleeve 12, heat exchange filling 13, puff prot 14.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.
Referring to Fig.1, a kind of chemical industry high-performance heat exchanger, including gas inlet tube 1, gas outlet 2, water inlet tube 3, water go out liquid
Pipe 4 and heat exchange fill 13, and gas inlet tube 1, gas outlet 2 penetrate through and be connected to the upper end that heat exchange fills 13, and water inlet tube 3, water go out
The perforation of liquid pipe 4 is connected to heat exchange and fills on 13 side walls, which is characterized in that water inlet tube 3 and water outlet tube 4 fill 13 by being located at heat exchange
A piece major flow duct 5 of inner cavity connects with each other, and heat exchange fills the cylinder thermal vias 6 that casting on 13 forms front and back intercommunication；
The both ends of the Zhi Liuguan 9 of a side wall perforation piece circulating reflux of grafting for major flow duct 5, and the other side of Zhi Liuguan 9
Equipped with heat dissipation tank 10, Zhi Liuguan 9 is wound on the side wall of heat dissipation tank 10, and the bottom of heat dissipation tank 10 is connected to heat exchange by spring 11
13 inner cavity lower curtate is filled, and the side wall perforation of heat dissipation tank 10 is connected with multiple puff prots 14, and the opening spray of puff prot 14 is located at
Between 8 crack of multiple heat-conducting blocks that 5 side wall of major flow duct is connected, the inner cavity upper end perforation of heat dissipation tank 10 is connected with sleeve 12,
And sliding plug has gas inlet tube 1 in sleeve 12.
The surface of internal cavity of cylinder thermal vias 6 is connected with multiple heat dissipation convex blocks 7, heat-conducting block 8 and puff prot 14 at least ten
Six, and equidistantly distributed, the bottom that heat exchange fills 13 is connected with universal wheel, easy to remove, Zhi Liuguan 9 slide up and down be wrapped in it is scattered
10 surface of hot tank.
Operation principle：This heat exchanger apparatus is intake by water inlet tube 3, water by major flow duct 5 and Zhi Liuguan 9 using
Water outlet tube 4 flows out, wherein and hot gas enters gas inlet tube 1, heat dissipation tank 10 is ejected into multiple heat-conducting blocks 8 from puff prot 14, into
Row heat exchange, moreover, air-flow drives the flutter up and down under the action of spring 11 of entire heat dissipation tank 10, so that heat dissipation tank 10
Heat can uniformly and effectively pass on Zhi Liuguan 9, prevent heat build-up, and on the other hand, cylinder thermal vias 6 can be by major flow
5 heat of pipe is taken away, and heat dissipation convex block 7 further expands heat dissipation area.
Described in this specification above content is only to the utility model example explanation.The utility model
Person of ordinary skill in the field can make various modifications or additions to the described embodiments or use class
As mode substitute, content without departing from the utility model specification or surmount model defined in the claims
It encloses, all should belong to the protection range of the utility model.
Claims (5)
1. a kind of chemical industry high-performance heat exchanger, including gas inlet tube (1), gas outlet (2), water inlet tube (3), water outlet tube
(4) and heat exchange fills (13), and gas inlet tube (1), gas outlet (2) penetrate through and be connected to the upper end that heat exchange fills (13), water feed liquor
Pipe (3), water outlet tube (4) perforation are connected to heat exchange and fill on (13) side wall, which is characterized in that the water inlet tube (3) and water go out
The major flow duct (5) that liquid pipe (4) fills (13) inner cavity by being located at heat exchange connects with each other, and the heat exchange fills pours on (13)
Cast at front and back intercommunication cylinder thermal vias (6)；
The both ends of the Zhi Liuguan (9) of a side wall perforation piece circulating reflux of grafting for the major flow duct (5), and Zhi Liuguan (9)
The other side is equipped with heat dissipation tank (10), and Zhi Liuguan (9) is wound on the side wall of heat dissipation tank (10), and the bottom of the heat dissipation tank (10) is logical
It crosses spring (11) and is connected to the inner cavity lower curtate that heat exchange fills (13), and the side wall perforation of heat dissipation tank (10) is connected with multiple puff prots
(14), and the spray of the opening of puff prot (14) is located between multiple heat-conducting blocks (8) crack that major flow duct (5) side wall is connected, institute
The inner cavity upper end perforation for stating heat dissipation tank (10) is connected with sleeve (12), and sliding plug has gas inlet tube (1) in sleeve (12).
2. a kind of chemical industry high-performance heat exchanger according to claim 1, which is characterized in that the cylinder thermal vias (6)
Surface of internal cavity be connected with multiple heat dissipation convex blocks (7).
3. a kind of chemical industry high-performance heat exchanger according to claim 1, which is characterized in that the heat-conducting block (8) and jet
Mouth (14) at least 16, and equidistantly distributed.
4. a kind of chemical industry high-performance heat exchanger according to claim 1, which is characterized in that the heat exchange fills the bottom of (13)
It is connected with universal wheel.
5. a kind of chemical industry high-performance heat exchanger according to claim 1, which is characterized in that glide on the Zhi Liuguan (9)
It is dynamic to be wrapped in heat dissipation tank (10) surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820418843.7U CN208075653U (en) | 2018-03-26 | 2018-03-26 | Chemical industry high-performance heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820418843.7U CN208075653U (en) | 2018-03-26 | 2018-03-26 | Chemical industry high-performance heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208075653U true CN208075653U (en) | 2018-11-09 |
Family
ID=64047929
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820418843.7U Expired - Fee Related CN208075653U (en) | 2018-03-26 | 2018-03-26 | Chemical industry high-performance heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208075653U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109612139A (en) * | 2018-12-03 | 2019-04-12 | 湖南达道新能源开发有限公司 | A kind of U-shaped well underground heat mixed flow heat exchange cycle system |
-
2018
- 2018-03-26 CN CN201820418843.7U patent/CN208075653U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109612139A (en) * | 2018-12-03 | 2019-04-12 | 湖南达道新能源开发有限公司 | A kind of U-shaped well underground heat mixed flow heat exchange cycle system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181109 Termination date: 20190326 |