CN102706184A - Immersive heat exchanger - Google Patents
Immersive heat exchanger Download PDFInfo
- Publication number
- CN102706184A CN102706184A CN2012101258473A CN201210125847A CN102706184A CN 102706184 A CN102706184 A CN 102706184A CN 2012101258473 A CN2012101258473 A CN 2012101258473A CN 201210125847 A CN201210125847 A CN 201210125847A CN 102706184 A CN102706184 A CN 102706184A
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- Prior art keywords
- heat exchanger
- container
- tank
- tube
- heat exchange
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- 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.)
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Abstract
An immersive heat exchanger comprises a container and a heat exchange tube arranged in the container. A feeding tube and a discharging tube of the heat exchange tube penetrate through container walls and extend to the outside of the container, a liquid inlet is arranged at the lower end of the container, a liquid outlet is arranged at the upper end of a face, which is opposite to the liquid inlet, of the container, the cross section of the heat exchange tube is square, the feeding tube is arranged on the container wall and positioned on the same horizontal level with the liquid outlet, the discharging tube is arranged on the container wall and is positioned on the same horizontal level with the liquid inlet, and the heat exchange tube is spirally wound. When the cross section of the container is square, the heat exchange tube is squarely arranged from a vertical view, and when the cross section of the container is circular, the heat exchange tube is circularly arranged from the vertical view. The immersive heat exchanger has the advantages that container volume can be increased, and utilization ratio of heat exchange liquid in the container is improved.
Description
Technical field
The present invention relates to the immersion heat exchanger, belong to chemical field.
Background technology
The immersion heat exchanger is the ripe heat exchanger of current application, in order to reach the time that prolongs heat exchange, normally heat-exchange tube is made the coiling shape, Here it is usually said coil heat exchanger.Coil heat exchanger can be that to make with the center of circle be the center, the concentric circles that spreads apart from inside to outside, and the mosquito-repellent incense shape of similar peviform can also be made spring-like, prolongs the time of staying of fluid in heat-exchange tube of treating heat exchange.But the immersion heat exchanger is immersed in the big volume, just makes that extratubal fluid is a lot, and tube fluid is few, and heat-transfer effect is undesirable.
Summary of the invention
In order to solve the problem of above existence, the invention discloses a kind of immersion heat exchanger, this immersion heat exchanger can increase tube fluid volume and extratubal fluid volume ratio, makes full use of volume and exchange liquid.
This immersion heat exchanger comprises tank and the heat exchanger tube that is arranged in the tank the inside, and the feed pipe of said heat exchanger tube and discharge nozzle pass the tank wall, reach the outside of tank, and the tank lower end is provided with inlet, and the upper end of the opposite face of inlet is provided with liquid outlet; The cross section of said heat exchanger tube is a square.
Said feed pipe is arranged on the tank wall with liquid outlet par height, and said discharge nozzle setting is on the tank wall of inlet par height.
Said heat exchanger tube is coiling shape in the shape of a spiral.
The cross section of said tank is a square, and described heat exchanger tube vertical view is square and arranges.
The cross section of said tank is circular, and the vertical view of said heat exchanger tube is circular.
The cross section of the heat exchanger tube of this immersion heat exchanger is square, and heat exchanger tube can be arranged closely, and the ratio that accounts for tank is just big, like this can be in the utilization rate of raising tank and tank the exchange efficiency of heat exchanger fluid.
Description of drawings
Fig. 1 is the structural representation of facing of the present invention,
Fig. 2 is top plan view of the present invention (view of embodiment 1),
Fig. 3 is top plan view of the present invention (view of embodiment 2),
Accompanying drawing is indicated tabulation: 1-tank, 2-liquid outlet, 3-feed pipe, 4-inlet, 5-discharge nozzle, 6-heat exchanger tube.
The specific embodiment
Below in conjunction with the accompanying drawing and the specific embodiment, further illustrate the present invention, should understand the following specific embodiment only be used to the present invention is described and be not used in the restriction scope of the present invention.Need to prove; Describe below the word " preceding " that uses, " back ", " left side ", " right side ", " on " and D score refer to the direction in the accompanying drawing, word " interior " and " outward " refer to respectively towards or away from the direction of specific features geometric center.
Fig. 1 is a structural representation of the present invention, and dotted line is represented the tank internals, as can be seen from the figure; This immersion heat exchanger; Comprise tank 1 and the heat exchanger tube 6 that is arranged in tank 1 the inside, the feed pipe 3 and the discharge nozzle 5 of heat exchanger tube 6 pass the tank wall, reach the outside of tank 1; Tank 1 lower end is provided with inlet 4, and the upper end of the opposite face of inlet 4 is provided with liquid outlet 2; Feed pipe 3 is arranged on the tank wall with liquid outlet 2 par height, and discharge nozzle 5 is provided with and is that heat exchanger tube 6 is coiling shape in the shape of a spiral on the tank wall of inlet 4 par height.
Embodiment 2, and is as shown in Figure 3, and Fig. 3 is a top plan view of the present invention, and the cross section of tank 1 is circular, and is rounded in the vertical view of heat exchanger tube 6.
According to the shape of tank 1, conversion heat exchanger tube 6 is coiled in the shape in the tank, reaches and rationally utilizes tank 1, reaches optimal heat exchanger effectiveness.
The cross section of heat exchanger tube 6 is a square, also is for the coiling of reasonable Arrangement in coiling process gap.
The disclosed technological means of the present invention program is not limited only to the disclosed technological means of above-mentioned technological means, also comprises the technical scheme of being made up of above technical characterictic combination in any.
Claims (5)
1. immersion heat exchanger; Comprise tank and the heat exchanger tube that is arranged in the tank the inside, it is characterized in that the feed pipe of said heat exchanger tube and discharge nozzle pass the tank wall, reach the outside of tank; The tank lower end is provided with inlet, and the upper end of the opposite face of inlet is provided with liquid outlet; The cross section of said heat exchanger tube is a square.
2. immersion heat exchanger according to claim 1 is characterized in that said feed pipe is arranged on the tank wall with liquid outlet par height, and said discharge nozzle setting is on the tank wall of inlet par height.
3. immersion heat exchanger according to claim 2 is characterized in that said heat exchanger tube is coiling shape in the shape of a spiral.
4. immersion heat exchanger according to claim 3 is characterized in that the cross section of said tank is square, and described heat exchanger tube vertical view is square and arranges.
5. immersion heat exchanger according to claim 3, the cross section that it is characterized in that said tank is for circular, and the vertical view of said heat exchanger tube is circular.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101258473A CN102706184A (en) | 2012-04-26 | 2012-04-26 | Immersive heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101258473A CN102706184A (en) | 2012-04-26 | 2012-04-26 | Immersive heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102706184A true CN102706184A (en) | 2012-10-03 |
Family
ID=46899137
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012101258473A Pending CN102706184A (en) | 2012-04-26 | 2012-04-26 | Immersive heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102706184A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103486775A (en) * | 2013-10-01 | 2014-01-01 | 王科伟 | Heat conduction structure of air conditioner and air conditioner |
| CN103644002A (en) * | 2013-11-29 | 2014-03-19 | 广西博宣食品有限公司 | Steam extraction cooling system of turbine steam seal for sugar factory |
| CN105202960A (en) * | 2015-10-10 | 2015-12-30 | 安陆火凤凰铝材有限责任公司 | Aluminum tube type heat exchanger |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB962837A (en) * | 1962-03-17 | 1964-07-08 | Ames Crosta Mills & Company Lt | Improvements in or relating to heat-exchangers |
| US4458138A (en) * | 1980-12-15 | 1984-07-03 | Adrian Glenn J | Fast recovery electric fluid |
| US5214927A (en) * | 1990-10-05 | 1993-06-01 | Squires David C | Method and apparatus for passive refrigerant and storage |
| CN101303213A (en) * | 2007-05-11 | 2008-11-12 | 湖南工业大学 | High-efficiency heat transfer device with heavy dirt type helical flow path structure |
-
2012
- 2012-04-26 CN CN2012101258473A patent/CN102706184A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB962837A (en) * | 1962-03-17 | 1964-07-08 | Ames Crosta Mills & Company Lt | Improvements in or relating to heat-exchangers |
| US4458138A (en) * | 1980-12-15 | 1984-07-03 | Adrian Glenn J | Fast recovery electric fluid |
| US5214927A (en) * | 1990-10-05 | 1993-06-01 | Squires David C | Method and apparatus for passive refrigerant and storage |
| CN101303213A (en) * | 2007-05-11 | 2008-11-12 | 湖南工业大学 | High-efficiency heat transfer device with heavy dirt type helical flow path structure |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103486775A (en) * | 2013-10-01 | 2014-01-01 | 王科伟 | Heat conduction structure of air conditioner and air conditioner |
| CN103486775B (en) * | 2013-10-01 | 2015-12-02 | 王科伟 | The heat conduction structure of air-conditioner and air-conditioner |
| CN103644002A (en) * | 2013-11-29 | 2014-03-19 | 广西博宣食品有限公司 | Steam extraction cooling system of turbine steam seal for sugar factory |
| CN105202960A (en) * | 2015-10-10 | 2015-12-30 | 安陆火凤凰铝材有限责任公司 | Aluminum tube type heat exchanger |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121003 |