CN202018210U - Hydrocyclone separation jet type cooling tower - Google Patents
Hydrocyclone separation jet type cooling tower Download PDFInfo
- Publication number
- CN202018210U CN202018210U CN2011201195507U CN201120119550U CN202018210U CN 202018210 U CN202018210 U CN 202018210U CN 2011201195507 U CN2011201195507 U CN 2011201195507U CN 201120119550 U CN201120119550 U CN 201120119550U CN 202018210 U CN202018210 U CN 202018210U
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- CN
- China
- Prior art keywords
- cooling tower
- cooling
- hydraulic separators
- cyclone hydraulic
- hydrocyclone separator
- 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 hydrocyclone separation jet type cooling tower, which comprises a cooling tower case, a multi-inlet hydrocyclone separator, an ejector, a cooling water pipeline and a water tank, wherein the multi-inlet hydrocyclone separator is arranged in the center of the cooling tower, the ejector is arranged on the periphery of the hydrocyclone separator and is connected with hydrocyclone separator inlets, the cooling water pipeline is surrounded around the hydrocyclone separator, and the water tank is arranged at the lower end of the hydrocyclone separator. The manufacture cost of the ejector and the hydrocyclone separator in the cooling tower is low, movable components such as a blower, a motor, a speed reducer and the like do not exist, the noise is reduced, and the maintenance cost and the repair cost are saved, so the whole manufacture cost of the cooling tower is low, and people only need to ensure that the cooling circulation water is required to keep clean in the maintenance work.
Description
Technical field
The utility model relates to the cooling tower technical field, relates in particular to a kind of injecting type cyclone hydraulic separators cooling tower.
Background technology
Cooling tower is an equipment of realizing the recirculated water cooling, generally just is used for handling a large amount of used heat that industrial processes produce, in industries such as metallurgy, oil, chemical industry, power, weaving acquisition extensive use.Though the cooling stack cooling effect is stable in the cooling tower that generally uses at present, the ventilation draft is little, is difficult for being used in hot and humid area.Though there are the serious loss of flying away in mechanical-draft cooling tower cooling effectiveness height, cooling water, wafing, it is big to ambient influnence to drip with fog.The problem of dripping though closed cooling tower good cooling results and nothing are waftd, owing to adopted the heat exchange property height in a large number but expensive copper tube coil, so the cost height.Present water resources shortage, the cooling tower that a kind of water saving, good cooling results and cost are low just is being that people are required.
The utility model content
The utility model is bad at existing natural aerating and cooling tower cooling effect, and mechanical-draft cooling tower is not economized on water, and the problem that the closed cooling tower cost is high is for the user provides a kind of water saving, good cooling results and cost low cooling tower.
The technical scheme that adopts of the present utility model is:
A kind of spinning liquid separation injection type cooling tower, comprise the cooling tower shell, be arranged on the multiple entry cyclone hydraulic separators at cooling tower center, be arranged in the injector that the cyclone hydraulic separators periphery is connected with spin liquid separator entrance, be looped around the cooling water pipeline of cyclone hydraulic separators periphery, be arranged on the tank of cyclone hydraulic separators lower end, described injector is connected with cooling water pipeline, the upper end of described cyclone hydraulic separators is provided with steam vent, and described tank is connected with cyclone hydraulic separators.
Cooling water and air carry out sufficient caloic exchange in the diffuser casing of injector, the cooling water enthalpy reduces, air enthalpy improves, air-water mixture enters cyclone hydraulic separators, utilize the centrifugal sedimentation principle to separate air-water mixture, hot-air is discharged outside the tower by cyclone hydraulic separators upper end steam vent, and recirculated cooling water is in falling into tank, flow out cooling tower through drainpipe, reach the good cooling effect.In the diffuser casing of injector, the violent hybrid perturbation of water smoke and air, spraying has formed the very big heat-transfer surface of formation between a large amount of fine drop and the cold air, in the time of contact heat-exchanging, water smoke constantly evaporates, and the water of evaporation has been drawn heat of vaporization from unevaporated water, so the thermic load in the water is transferred in the air dielectric, cooling water temperature reduces; In cyclone hydraulic separators, approach saturated air and be fully loaded with heat outside the steam vent effusion tower on cyclone hydraulic separators top, the cooling water rotation sinks to entering tank, and not having wafts drips phenomenon.Because injector and cyclone hydraulic separators cost are low in the cooling tower, do not have movable parts such as blower fan, motor, reductor, reduced noise, saved the maintenance cost maintenance cost, so the cooling tower overall cost is low, in maintenance work, need only the cleaning of noting keeping cooling circulating water.
Description of drawings
Fig. 1 is a front view of the present utility model;
Fig. 2 is a vertical view of the present utility model.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
As illustrated in fig. 1 and 2, a kind of spinning liquid separation injection type cooling tower, comprise the cooling tower shell, be arranged on the multiple entry cyclone hydraulic separators 2 at cooling tower center, be arranged in the injector 1 that the cyclone hydraulic separators periphery is connected with spin liquid separator entrance, be looped around the cooling water pipeline of cyclone hydraulic separators periphery, be arranged on the tank 3 of cyclone hydraulic separators lower end, described injector 1 is connected with cooling water pipeline, the upper end of described cyclone hydraulic separators 2 is provided with steam vent, and described tank 3 is positioned at the cyclone hydraulic separators lower end, and cooling water enters injector 1 through cooling water pipeline, carry out sufficient caloic exchange with the driving fluid air in injector 1, cooling water temperature reduces.The gas-liquid mixture fluid that goes out injector 1 enters cyclone hydraulic separators 2, in cyclone hydraulic separators 2, separate air-water mixture according to the centrifugal sedimentation principle, hot-air is discharged outside the tower by cyclone hydraulic separators 2 upper end steam vents, recirculated cooling water is in falling into tank 3, flow out cooling tower through drainpipe, reach cooling-down effect.
Cooling water and air have carried out sufficient caloic exchange in injector 1, cooling water temperature reduces; The cooling water rotation sinks to entering tank 3 in cyclone hydraulic separators 2, and hot-air is discharged by the aperture, top, and not having wafts drips phenomenon.Because injector and cyclone hydraulic separators cost are low in the cooling tower, do not have movable parts such as blower fan, motor, reductor, have reduced noise, have saved the maintenance cost maintenance cost.
More than show and described basic principle of the present utility model, principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that describes in the foregoing description and the specification just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (1)
1. spinning liquid separation injection type cooling tower, it is characterized in that, comprise the cooling tower shell, be arranged on the multiple entry cyclone hydraulic separators at cooling tower center, be arranged in the injector that the cyclone hydraulic separators periphery is connected with spin liquid separator entrance, be looped around the cooling water pipeline of cyclone hydraulic separators periphery, be arranged on the tank of cyclone hydraulic separators lower end, described injector is connected with cooling water pipeline, and the upper end of described cyclone hydraulic separators is provided with steam vent, and described tank is connected with cyclone hydraulic separators.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201195507U CN202018210U (en) | 2011-04-21 | 2011-04-21 | Hydrocyclone separation jet type cooling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201195507U CN202018210U (en) | 2011-04-21 | 2011-04-21 | Hydrocyclone separation jet type cooling tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202018210U true CN202018210U (en) | 2011-10-26 |
Family
ID=44811879
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201195507U Expired - Fee Related CN202018210U (en) | 2011-04-21 | 2011-04-21 | Hydrocyclone separation jet type cooling tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202018210U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102128549A (en) * | 2011-04-21 | 2011-07-20 | 上海海事大学 | Hydrocyclone separation jet cooling tower |
-
2011
- 2011-04-21 CN CN2011201195507U patent/CN202018210U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102128549A (en) * | 2011-04-21 | 2011-07-20 | 上海海事大学 | Hydrocyclone separation jet cooling tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111026 Termination date: 20120421 |