CN206257865U - A kind of Coal Chemical Industry cooling device - Google Patents
A kind of Coal Chemical Industry cooling device Download PDFInfo
- Publication number
- CN206257865U CN206257865U CN201621373139.1U CN201621373139U CN206257865U CN 206257865 U CN206257865 U CN 206257865U CN 201621373139 U CN201621373139 U CN 201621373139U CN 206257865 U CN206257865 U CN 206257865U
- Authority
- CN
- China
- Prior art keywords
- pipe
- heat exchanger
- water
- exchanger fin
- heat
- 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 kind of Coal Chemical Industry cooling device,Including water tank,Top water pond,Bottom water pond,Heat exchanger fin,Heat conducting pipe and recovery tank,Water supply pump is connected between the water tank and the top water pond,The heat conducting pipe is connected between the top water pond and the bottom water pond,The heat conducting pipe annular is provided with more than three,The heat exchanger fin is arranged between the top water pond and the bottom water pond,The heat exchanger fin is arranged with more than three in parallel,The surface of the heat exchanger fin is provided with the hole passed through for the heat conducting pipe,The heat conducting pipe and the hole interference fits,The bottom water pond is connected with drainpipe,The branched pipe of more than one is provided with the pipe shaft of the drainpipe,The branched pipe connects the recovery tank,The water tank is connected with return pipe,The return pipe is connected with the first branched pipe,First branched pipe connects the recovery tank；The present apparatus can improve heat transfer rate, can increase cooling effect.
Description
Technical field
The utility model is related to a kind of Coal Chemical Industry cooling device.
Background technology
Converted for Coal Chemical Industry, coking coal gas, gas generator production coal gas enterprise, or coal gas production process
Using enterprise, often, it is necessary to carry out safe cooling to coal gas during coal gas use.
The existing type of cooling is mainly water-cooled, but the cooling effect by way of water pipe direct heat transfer is more low
Under.
The content of the invention
The technical problems to be solved in the utility model is to provide a kind of raising heat transfer rate, can increase the coalification of cooling effect
Work cooling device.
To solve the above problems, the utility model is adopted the following technical scheme that：
A kind of Coal Chemical Industry cooling device, including water tank, top water pond, bottom water pond, heat exchanger fin, heat conducting pipe and recovery tank,
Be connected with water supply pump between the water tank and the top water pond, the heat conducting pipe be connected to the top water pond and it is described under
Between portion's water pond, the heat conducting pipe annular is provided with more than three, the heat exchanger fin be arranged at the top water pond and it is described under
Between portion's water pond, the heat exchanger fin is arranged with more than three in parallel, and the surface of the heat exchanger fin is provided with wears for the heat conducting pipe
The hole crossed, the heat conducting pipe and the hole interference fits, the bottom water pond is connected with drainpipe, on the pipe shaft of the drainpipe
The branched pipe of more than one is provided with, the branched pipe connects the recovery tank, first is provided with the pipe shaft of the branched pipe
Control valve, the water tank is connected with return pipe, and the return pipe is connected with the first branched pipe, and first branched pipe connects institute
Recovery tank is stated, the second control valve is provided with the pipe shaft of first branched pipe.
Preferably, heat-insulated cotton pad is provided with the inner wall position of the top water pond, the thickness of the heat-insulated cotton pad is not small
In 8mm, the heat absorption of top water pond can be reduced by heat-insulated cotton pad.
Preferably, the surface of the heat exchanger fin is evenly equipped with louvre, and the louvre vertically runs through the heat exchanger fin, described
Heat exchanger fin is copper piece or aluminum piece, and the thickness of the heat exchanger fin is 1mm-1.5mm, by louvre can increase heat exchanger fin with
The contact area of air, increases heat dissipation capacity.
Preferably, the recovery tank is stainless steel water tank, and the wall thickness of the recovery tank is 1mm-1.6mm, the recovery tank
Outer wall at be provided with more than two panels radiating fin, weld solid between the radiating fin and the recovery tank more than two panels
It is fixed, the cooling capacity of recovery tank can be increased by radiating fin, improve operating efficiency.
Preferably, overflow pipe is provided with the close tip position of the backwater box outer wall, will can be returned by overflow pipe
Vapor discharge in water tank, it is to avoid exploded caused by pressure in recovery tank is excessive.
Preferably, electronic thermometer is provided with the top of the water tank, the measurement end of the electronic thermometer extends to institute
State in water tank, the water temperature in water tank can be monitored by electronic thermometer, when water temperature over-high, close combustion chamber, treat water tank temperature
Degree works on after declining.
Preferably, water inlet pipe is provided with the close tip position of the water tank, moisturizing can be carried out by water inlet pipe.
The beneficial effects of the utility model are：Heat exchanger fin is coated on the present apparatus outside of combustion chamber when in use, is passed through
Heat exchanger fin collects the heat of combustion chamber, increases rate of heat exchange, and the heat on heat exchanger fin surface then is passed through into water-cooled by heat conducting pipe
Mode take away, effectively reduce the heat of combustion chamber, the water after heat absorption is contained to recovery tank, is closed after recovery tank water storage is full
The first control valve is closed, water is drained into the utilization of water tank interior circulation after the second control valve is opened after water cooling, it is multiple by setting
, to meet various sizes of combustion chamber cooling needs, the structure of the present apparatus is relatively simple, and cost is more cheap for recovery tank, install compared with
For convenience, it is adapted to promote the use of.
Brief description of the drawings
In order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, is not paying the premise of creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the upward view of top water pond；
Fig. 3 is the top view of heat exchanger fin.
Specific embodiment
Preferred embodiment of the present utility model is described in detail below in conjunction with the accompanying drawings, so that advantage of the present utility model
Can be easier to be readily appreciated by one skilled in the art with feature, it is apparent clear and definite so as to be made to protection domain of the present utility model
Define.
Refering to a kind of Coal Chemical Industry cooling device shown in Fig. 1, Fig. 2 and Fig. 3, including water tank 1, top water pond 2, bottom water pond
3rd, heat exchanger fin 4, heat conducting pipe 5 and recovery tank 6, are connected with water supply pump 7 between the water tank 1 and the top water pond 2, described to lead
Heat pipe 5 is connected between the top water pond 2 and the bottom water pond 3, and the annular of the heat conducting pipe 5 is provided with more than three, institute
Heat exchanger fin 4 is stated to be arranged between the top water pond 2 and the bottom water pond 3, the heat exchanger fin 4 be arranged with parallel three with
On, the surface of the heat exchanger fin 4 is provided with the hole 401 passed through for the heat conducting pipe 5, the heat conducting pipe 5 and the transition of the hole 401
Coordinate, the bottom water pond 3 is connected with drainpipe 8, the branched pipe 9 of more than, institute are provided with the pipe shaft of the drainpipe 8
State branched pipe 9 and connect the recovery tank 6, the first control valve 901 is provided with the pipe shaft of the branched pipe 9, the water tank 1 connects
Return pipe 10 is connected to, the return pipe 10 is connected with the first branched pipe 11, and first branched pipe 11 connects the recovery tank 6,
The second control valve 12 is provided with the pipe shaft of first branched pipe 11.
A preferred embodiment in the utility model, heat-insulated cotton pad is provided with the inner wall position of the top water pond 2
211, the thickness of the heat-insulated cotton pad 211 is 12mm, and the heat absorption of top water pond can be reduced by heat-insulated cotton pad.
A preferred embodiment in the utility model, the surface of the heat exchanger fin 4 is evenly equipped with louvre 441, described to dissipate
Hot hole 441 vertically runs through the heat exchanger fin 4, and the heat exchanger fin 4 is copper piece, and the thickness of the heat exchanger fin 4 is 1.5mm, is passed through
Louvre can increase the contact area of heat exchanger fin and air, increase heat dissipation capacity.
A preferred embodiment in the utility model, the recovery tank 6 is stainless steel water tank, the wall thickness of the recovery tank
It is 1.6mm, radiating fin 661 more than two panels is provided with the outer wall of the recovery tank 6, the radiating fin more than two panels
It is welded and fixed between 661 and the recovery tank 6, the cooling capacity of recovery tank can be increased by radiating fin, improves work effect
Rate.
A preferred embodiment in the utility model, is provided with excessive at the close tip position of the outer wall of the recovery tank 6
Water pipe 62, can be discharged the vapor in recovery tank 6 by overflow pipe 662, it is to avoid the pressure in recovery tank 6 is excessive and causes
Blast.
A preferred embodiment in the utility model, the top of the water tank 1 is provided with electronic thermometer 121, described
The measurement end of electronic thermometer 121 is extended in the water tank 1, and the water temperature in water tank can be monitored by electronic thermometer, when
During water temperature over-high, combustion chamber is closed, worked on after after water tank temperature decline.
A preferred embodiment in the utility model, water inlet pipe is provided with the close tip position of the water tank 1
131, moisturizing can be carried out by water inlet pipe.
The beneficial effects of the utility model are：Heat exchanger fin is coated on the present apparatus outside of combustion chamber when in use, is passed through
Heat exchanger fin collects the heat of combustion chamber, increases rate of heat exchange, and the heat on heat exchanger fin surface then is passed through into water-cooled by heat conducting pipe
Mode take away, effectively reduce the heat of combustion chamber, the water after heat absorption is contained to recovery tank, is closed after recovery tank water storage is full
The first control valve is closed, water is drained into the utilization of water tank interior circulation after the second control valve is opened after water cooling, it is multiple by setting
, to meet various sizes of combustion chamber cooling needs, the structure of the present apparatus is relatively simple, and cost is more cheap for recovery tank, install compared with
For convenience, it is adapted to promote the use of.
General principle of the present utility model, principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, the utility model can also on the premise of the utility model spirit and scope are not departed from
There are various changes and modifications, these changes and improvements are both fallen within the range of claimed the utility model.The utility model will
Protection domain is asked to be defined by appending claims and its equivalent.
Claims (7)
1. a kind of Coal Chemical Industry cooling device, it is characterised in that：Including water tank, top water pond, bottom water pond, heat exchanger fin, heat conducting pipe
And recovery tank, water supply pump is connected between the water tank and the top water pond, the heat conducting pipe is connected to the upper water
Between disk and the bottom water pond, the heat conducting pipe annular is provided with more than three, and the heat exchanger fin is arranged at the upper water
Between disk and the bottom water pond, the heat exchanger fin is arranged with more than three in parallel, and the surface of the heat exchanger fin is provided with and supplies institute
The hole that heat conducting pipe is passed through, the heat conducting pipe and the hole interference fits are stated, the bottom water pond is connected with drainpipe, the draining
The branched pipe of more than one is provided with the pipe shaft of pipe, the branched pipe connects the recovery tank, on the pipe shaft of the branched pipe
The first control valve is provided with, the water tank is connected with return pipe, and the return pipe is connected with the first branched pipe, described first point
Branch pipe connects the recovery tank, and the second control valve is provided with the pipe shaft of first branched pipe.
2. Coal Chemical Industry cooling device according to claim 1, it is characterised in that：Set at the inner wall position of the top water pond
Heat-insulated cotton pad is equipped with, the thickness of the heat-insulated cotton pad is not less than 8mm.
3. Coal Chemical Industry cooling device according to claim 1, it is characterised in that：The surface of the heat exchanger fin is evenly equipped with radiating
Hole, the louvre vertically runs through the heat exchanger fin, and the heat exchanger fin is copper piece or aluminum piece, and the thickness of the heat exchanger fin is
1mm-1.5mm。
4. Coal Chemical Industry cooling device according to claim 1, it is characterised in that：The recovery tank is stainless steel water tank, institute
The wall thickness of recovery tank is stated for 1mm-1.6mm, radiating fin more than two panels is provided with the outer wall of the recovery tank, more than two panels
The radiating fin and the recovery tank between be welded and fixed.
5. Coal Chemical Industry cooling device according to claim 1, it is characterised in that：The close top position of the backwater box outer wall
The place of putting is provided with overflow pipe.
6. Coal Chemical Industry cooling device according to claim 1, it is characterised in that：Electronics temperature is provided with the top of the water tank
Degree meter, the measurement end of the electronic thermometer is extended in the water tank.
7. Coal Chemical Industry cooling device according to claim 1, it is characterised in that：Set at the close tip position of the water tank
It is equipped with water inlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621373139.1U CN206257865U (en) | 2016-12-14 | 2016-12-14 | A kind of Coal Chemical Industry cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621373139.1U CN206257865U (en) | 2016-12-14 | 2016-12-14 | A kind of Coal Chemical Industry cooling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206257865U true CN206257865U (en) | 2017-06-16 |
Family
ID=59028397
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621373139.1U Expired - Fee Related CN206257865U (en) | 2016-12-14 | 2016-12-14 | A kind of Coal Chemical Industry cooling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206257865U (en) |
-
2016
- 2016-12-14 CN CN201621373139.1U patent/CN206257865U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20170616 Termination date: 20171214 |