CN207501725U - Tower evaporation condenser - Google Patents
Tower evaporation condenser Download PDFInfo
- Publication number
- CN207501725U CN207501725U CN201721565465.7U CN201721565465U CN207501725U CN 207501725 U CN207501725 U CN 207501725U CN 201721565465 U CN201721565465 U CN 201721565465U CN 207501725 U CN207501725 U CN 207501725U
- Authority
- CN
- China
- Prior art keywords
- condenser
- spray column
- tower
- reading
- wall
- 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
Links
- 238000001704 evaporation Methods 0.000 title claims abstract description 13
- 230000008020 evaporation Effects 0.000 title claims abstract description 13
- 239000007921 spray Substances 0.000 claims abstract description 58
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000011229 interlayer Substances 0.000 claims abstract description 6
- 238000009423 ventilation Methods 0.000 claims abstract description 5
- 238000009833 condensation Methods 0.000 claims description 7
- 230000005494 condensation Effects 0.000 claims description 7
- 230000017525 heat dissipation Effects 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model belongs to condenser technology field, specially tower evaporation condenser, is hollow structure including spray column, inside spray column, the side wall of spray column is sandwich, is water stream channel in interlayer；Multiple nozzles are provided on spray inner wall of tower；To be round suitable for reading, low side is round lower mouth on spray column top, air duct be mounted on the circle described in spray column it is suitable for reading on, the lower mouth of circle is connected with the barrel support with ventilation opening；Condenser is mounted in the interior hollow section and barrel support of spray column, and there are air ducts between the inner wall of the inner wall of condenser and spray column, barrel support；Catch basin is mounted below condenser；The round intake chamber suitable for reading for being additionally provided with annular；Condenser includes the pyramidal structure at top and the cylindrical structure of bottom.Tower evaporation condenser provided by the utility model, the condenser of turriform increase heat dissipation area, extend the heat dissipation time, improve heat dissipation effect, saved the energy.
Description
Technical field
The utility model belongs to condenser technology field, specially tower evaporation condenser.
Background technology
Evaporative condenser integrates water-cooled condenser, cooling tower, water pump, collecting-tank, has water loss few, takes up an area
The advantages that space is relatively small, the fields such as extensive use and refrigeration, air-conditioning, chemical industry.
Wherein, without the evaporative condenser of filler due to not having filler, in condenser portion, the heat exchange of air and water is adopted
With countercurrent flow, the cooling water of water place one's entire reliance upon lower leaching water with air is skyborne contacts, the heat exchange of air and water can only
It completes in the air, since water is small with air contact area, heat transfer effect is not obvious.The water of higher temperatures is directly entered collecting-tank,
Make to catchment the temperature raising of pool inner water, and the temperature for spraying water on condenser is higher, and heat exchange efficiency is low, high energy consumption.
Utility model content
For above-mentioned technical problem, the utility model provides a kind of good effect of heat exchange, the tower evaporation condenser that low energy consumption.
Specifically technical solution is：
Tower evaporation condenser, condenser, the catch basin formed including condensation fan, by tube bank and fin；Further include spray
Tower is drenched, is hollow structure inside spray column, the side wall of spray column is sandwich, is water stream channel in interlayer；
Multiple nozzles are provided on spray inner wall of tower；Nozzle is towards the interior hollow section of spray column；
To be round suitable for reading, low side is round lower mouth on the spray column top, and circle internal diameter suitable for reading is less than circle
The internal diameter of mouth under shape, the condensation fan are mounted on by supporting rod in air duct, and the air duct is mounted on described in spray column
Circle it is suitable for reading on, mouth is connected with the barrel support with ventilation opening under the circle；
The condenser is mounted in the interior hollow section and barrel support of spray column, and condenser and spray column
Inner wall, barrel support inner wall between there are air ducts；
The catch basin is mounted below condenser；The circle intake chamber suitable for reading for being additionally provided with annular.It is described
The pyramidal structure of condenser including top and the cylindrical structure of bottom；The axial line of condenser and the axial line weight of spray column
It closes.
Further, the side wall of the pyramidal structure described in condenser is set as the step state of multilayer.
Further, the side wall of spray column is bent to spray column inner axes line, and the side wall of corresponding condenser is to turriform knot
Structure inner axes line is bent.
Tower evaporation condenser provided by the utility model, hot water are entered in the interlayer of the side wall of spray column, on to
Under trickling during, the side wall of spray column is made, such as metal using the preferable material of heat conductivility, during trickling,
Part heat can be dissipated, while water is sprayed onto from the inner wall spout of spray column in spray column inner cavity, during spray, hot water exists
By the air draft of wind turbine in tower, continue to disperse a part of heat, then fall on the condenser of bottom, radiate again, tower
The condenser of shape, increases heat dissipation area, extends the heat dissipation time, improves heat dissipation effect, saved the energy.
Description of the drawings
Fig. 1 is the cross-sectional view of the utility model.
Specific embodiment
It is described in conjunction with the embodiments specific embodiment of the present utility model.
As shown in Figure 1, tower evaporation condenser, the condenser formed including condensation fan 1, by tube bank and fin catchment
Slot 7；Spray column 4 is further included, 4 inside of spray column is hollow structure, and the side wall of spray column 4 is sandwich, and side wall is thermal conductivity
The preferable material of energy is made, such as copper, is water stream channel in interlayer, when water passes through water stream channel, can be carried out by side wall
Heat dissipation.
Multiple nozzles 5 are provided on 4 inner wall of spray column；Nozzle 5 towards spray column 4 interior hollow section, by spray column 4
Water in interlayer is sprayed onto hollow region in tower.
To be round suitable for reading, low side is round lower mouth on 4 top of spray column, and circle internal diameter suitable for reading is less than circle
The internal diameter of mouth under shape, the condensation fan 1 are mounted on by supporting rod in air duct 2, and the air duct 2 is mounted on spray column 4
On the circle is suitable for reading, mouth is connected with the barrel support 6 with ventilation opening under the circle；
The condenser is mounted in the interior hollow section and barrel support 6 of spray column 4, and condenser and spray column
There are air ducts between 4 inner wall, the inner wall of barrel support 6；Ventilation opening on barrel support 6 is by the cold sky outside 4 bottom of spray column
Gas is imported into spray column 4, sprays the hot water in tower, and the heat and steam to shed is discharged by condensation fan 1 from top, then
Water is fallen on the condenser of lower section, is further cooled down.
The catch basin 7 is mounted below condenser；The circle intake chamber 3 suitable for reading for being additionally provided with annular.Ring
Shape water distribution can cause water to uniformly enter in spray column 4, and can control flow.
The condenser includes the pyramidal structure 8 at top and the cylindrical structure 10 of bottom；The axial line of condenser and spray
The axial line for drenching tower 4 overlaps.
The side wall 9 of pyramidal structure 8 described in condenser is set as the step state of multilayer.
Side wall 9 is step structure, can be rested on side wall 9, and smoothly enter turriform for the water of spray
In structure 8, water successively falls in pyramidal structure 8, finally enters cylindrical structure 10, due to 8 bottom of pyramidal structure and cylinder knot
Structure 10 is relatively large in diameter, and can adequately retain the water under spraying.
The side wall of spray column 4 is bent to 4 inner axes line of spray column, and the side wall 9 of corresponding condenser is to 8 inner shaft of pyramidal structure
Heart line is bent.Side wall 9 and the shape of the side wall of spray column 4 of condenser can be similar.
Side wall is arranged to concave inward structure, is the length in order to increase side wall first, increases side wall heat dissipation area, secondly, is
To enable the spray of inner wall upper nozzle multi-angle, the installation of spray port divergent shape, the flow sprayed out is also divergent state,
Increase the space that water radiates in the air.The side wall 9 of corresponding condenser is also for the area for increasing water receiving.
Claims (4)
1. tower evaporation condenser, including condensation fan（1）, by tube bank and the fin condenser, the catch basin that form（7）；It is special
Sign is, further includes spray column（4）, spray column（4）Hollow structure is in inside, spray column（4）Side wall for sandwich, interlayer
Interior is water stream channel；
Spray column（4）Multiple nozzles are provided on inner wall（5）；Nozzle（5）Towards spray column（4）Interior hollow section；
The spray column（4）To be round suitable for reading, low side is round lower mouth on top, and circle internal diameter suitable for reading is less than circle
The internal diameter of lower mouth, the condensation fan（1）Air duct is mounted on by supporting rod（2）Interior, described air duct（2）Mounted on spray
Tower（4）On the circle is suitable for reading, mouth is connected with the barrel support with ventilation opening under the circle（6）；
The condenser is mounted on spray column（4）Interior hollow section and barrel support（6）It is interior, and condenser and spray column
（4）Inner wall, barrel support（6）Inner wall between there are air ducts；
The condenser includes the pyramidal structure at top（8）With the cylindrical structure of bottom（10）；The axial line of condenser and spray
Drench tower（4）Axial line overlap；
The catch basin（7）Below condenser；The circle intake chamber suitable for reading for being additionally provided with annular（3）.
2. tower evaporation condenser according to claim 1, which is characterized in that the pyramidal structure described in condenser（8）'s
Side wall（9）It is set as the step state of multilayer.
3. tower evaporation condenser according to claim 1 or 2, which is characterized in that spray column（4）Side wall to spray column
（4）Inner axes line is bent.
4. tower evaporation condenser according to claim 3, which is characterized in that the side wall of the condenser（9）To tower
Shape structure（8）Inner axes line is bent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721565465.7U CN207501725U (en) | 2017-11-22 | 2017-11-22 | Tower evaporation condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721565465.7U CN207501725U (en) | 2017-11-22 | 2017-11-22 | Tower evaporation condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207501725U true CN207501725U (en) | 2018-06-15 |
Family
ID=62505254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721565465.7U Expired - Fee Related CN207501725U (en) | 2017-11-22 | 2017-11-22 | Tower evaporation condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207501725U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110665242A (en) * | 2019-10-18 | 2020-01-10 | 许良云 | Combined type methanol evaporator |
| CN114340329A (en) * | 2021-12-20 | 2022-04-12 | 曙光数据基础设施创新技术(北京)股份有限公司 | Cooling device |
-
2017
- 2017-11-22 CN CN201721565465.7U patent/CN207501725U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110665242A (en) * | 2019-10-18 | 2020-01-10 | 许良云 | Combined type methanol evaporator |
| CN110665242B (en) * | 2019-10-18 | 2022-07-01 | 临沂金朗化工有限公司 | Combined type methanol evaporator |
| CN114340329A (en) * | 2021-12-20 | 2022-04-12 | 曙光数据基础设施创新技术(北京)股份有限公司 | Cooling device |
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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: 20180615 Termination date: 20201122 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |