CN206369495U - A kind of phase-change type heat exchanger - Google Patents
A kind of phase-change type heat exchanger Download PDFInfo
- Publication number
- CN206369495U CN206369495U CN201621402676.4U CN201621402676U CN206369495U CN 206369495 U CN206369495 U CN 206369495U CN 201621402676 U CN201621402676 U CN 201621402676U CN 206369495 U CN206369495 U CN 206369495U
- Authority
- CN
- China
- Prior art keywords
- temperature inlet
- heat exchanger
- phase
- outlet pipeline
- mixing chamber
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of phase-change type heat exchanger, exchanged heat using two kinds of mutual exclusive working medium, including the hot outlet pipeline (1) set gradually from top to bottom, working medium collector (2), mixing chamber, isocon (5) and high temperature inlet pipe road (6), wherein, high temperature inlet pipe road (6) is connected by isocon (5) with mixing chamber, the low-temperature outlet pipeline (3) being connected and low temperature inlet ductwork (4) are provided with mixing chamber, and the position of low-temperature outlet pipeline (3) is higher than the position of low temperature inlet ductwork (4), hot outlet pipeline (1) is connected by working medium collector (2) with mixing chamber.The utility model can be safely and steadily run using two kinds of mutual exclusive working medium, good mixing effect, heat exchanger；There is phase transformation in heat transfer process, being capable of enhanced heat exchange.
Description
Technical field：
The utility model is related to a kind of phase-change type heat exchanger, is exchanged heat for two kinds of mutual exclusive working medium, and heat exchange
During there is phase transformation.
Background technology：
During heat exchanger is the essential equipment of thermal technology's industry, practical application, the heat exchange efficiency of heat exchanger often influence be
The safe operation of system.Traditional air-cooled and water cooling generally requires larger heat exchange area, increases the investment cost of equipment；Traditional
Although mixing, contact heat exchanger heat exchange efficiency is higher, is due to be readily incorporated impurity while more difficult point of the two media mixed
From, therefore it is also restrained in application process.
Utility model content：
The purpose of this utility model is to overcome above-mentioned deficiency to exchange heat there is provided a kind of efficient, safe and stable phase-change type
Device.
To reach above-mentioned purpose, the technical scheme that the utility model is used is：
A kind of phase-change type heat exchanger, including hot outlet pipeline, working medium collector, the hybrid chamber set gradually from top to bottom
Body, isocon and high temperature inlet pipe road, wherein, high temperature inlet pipe road is connected by isocon with mixing chamber, hybrid chamber
The low-temperature outlet pipeline being connected and low temperature inlet ductwork are provided with body, and the position of low-temperature outlet pipeline is higher than low temperature import
The position of pipeline, hot outlet pipeline is connected by working medium collector with mixing chamber.
The utility model, which is further improved, to be, high temperature inlet pipe road is used to be passed through vapor.
The utility model, which is further improved, to be, low temperature inlet ductwork is used to be passed through carbon tetrachloride liquid.
The utility model, which is further improved, to be, isocon uses thin straight tube or U-tube.
The utility model, which is further improved, to be, the internal diameter on high temperature inlet pipe road is less than the internal diameter of low temperature inlet ductwork,
The internal diameter of isocon is less than the internal diameter on high temperature inlet pipe road.
The utility model has following beneficial effect：
The utility model can be safely and steadily run using two kinds of mutual exclusive working medium, good mixing effect, heat exchanger.
Brief description of the drawings：
Fig. 1 is structural representation of the present utility model.
In figure：1- hot outlet pipelines；2- working medium collectors；3- low-temperature outlet pipelines；4- low temperature inlet ductworks；5- is shunted
Pipe；6- high temperature inlet pipes road.
Embodiment：
The utility model is described in further detail below in conjunction with accompanying drawing.
As shown in figure 1, a kind of phase-change type heat exchanger of the utility model, including the hot outlet pipe set gradually from top to bottom
Road 1, working medium collector 2, mixing chamber, isocon 5 and high temperature inlet pipe road 6, wherein, high temperature inlet pipe road 6 passes through shunting
Pipe 5 is connected with mixing chamber, and the low-temperature outlet pipeline 3 being connected and low temperature inlet ductwork 4 are provided with mixing chamber, and low
The position of warm export pipeline 3 is higher than the position of low temperature inlet ductwork 4, and hot outlet pipeline 1 passes through working medium collector 2 and hybrid chamber
Body phase is connected.
Wherein, isocon 5 uses thin straight tube or U-tube.In addition, the internal diameter on high temperature inlet pipe road 6 is less than low temperature import
The internal diameter of pipeline 4, the internal diameter of isocon 5 is less than the internal diameter on high temperature inlet pipe road 6, can be effective because the diameter of isocon 5 is smaller
Prevent the mixture of deep fat and water from flowing back.The density of the working medium (carbon tetrachloride liquid, but be not limited to carbon tetrachloride) of use is higher than
The density of aqueous water (being not limited to aqueous water), and with water (being not limited to aqueous water) objectionable intermingling.
During work, vapor is shunted by isocon 5, from the inflow heat exchanger of high temperature inlet pipe road 6, carbon tetrachloride liquid from
The inflow heat exchanger of low temperature inlet ductwork 4, after both mixing, fully heat exchange, because the density of carbon tetrachloride is more than water, carbon tetrachloride
It is aqueous water that liquid and aqueous water layering-vapor, which release heat liquefaction, is gathered in working medium collector 2, then goes out from high temperature
Mouthful outflow heat exchanger of pipeline 1, absorbs the carbon tetrachloride liquid of heat from the outflow heat exchanger of low-temperature outlet pipeline 3.
Claims (5)
1. a kind of phase-change type heat exchanger, it is characterised in that including set gradually from top to bottom hot outlet pipeline (1), working medium
Collector (2), mixing chamber, isocon (5) and high temperature inlet pipe road (6), wherein, high temperature inlet pipe road (6) pass through shunting
Pipe (5) is connected with mixing chamber, and the low-temperature outlet pipeline (3) being connected and low temperature inlet ductwork are provided with mixing chamber
(4), and the position of low-temperature outlet pipeline (3) is higher than the position of low temperature inlet ductwork (4), hot outlet pipeline (1) passes through working medium
Collector (2) is connected with mixing chamber.
2. a kind of phase-change type heat exchanger according to claim 1, it is characterised in that high temperature inlet pipe road (6) are used to be passed through
Vapor.
3. a kind of phase-change type heat exchanger according to claim 1, it is characterised in that low temperature inlet ductwork (4) is used to be passed through
Carbon tetrachloride liquid.
4. a kind of phase-change type heat exchanger according to claim 1, it is characterised in that isocon (5) uses thin straight tube or U
Shape pipe.
5. a kind of phase-change type heat exchanger according to claim 1, it is characterised in that the internal diameter of high temperature inlet pipe road (6) is small
Internal diameter in low temperature inlet ductwork (4), the internal diameter of isocon (5) is less than the internal diameter of high temperature inlet pipe road (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621402676.4U CN206369495U (en) | 2016-12-20 | 2016-12-20 | A kind of phase-change type heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621402676.4U CN206369495U (en) | 2016-12-20 | 2016-12-20 | A kind of phase-change type heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206369495U true CN206369495U (en) | 2017-08-01 |
Family
ID=59392978
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621402676.4U Expired - Fee Related CN206369495U (en) | 2016-12-20 | 2016-12-20 | A kind of phase-change type heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206369495U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109115020A (en) * | 2018-07-23 | 2019-01-01 | 山东理工大学 | A kind of method of phase boundary surface strengthening convective heat transfer |
-
2016
- 2016-12-20 CN CN201621402676.4U patent/CN206369495U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109115020A (en) * | 2018-07-23 | 2019-01-01 | 山东理工大学 | A kind of method of phase boundary surface strengthening convective heat transfer |
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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 |
Granted publication date: 20170801 Termination date: 20211220 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |