CN204202471U - Cooling tower droplet retracting device - Google Patents
Cooling tower droplet retracting device Download PDFInfo
- Publication number
- CN204202471U CN204202471U CN201420550903.2U CN201420550903U CN204202471U CN 204202471 U CN204202471 U CN 204202471U CN 201420550903 U CN201420550903 U CN 201420550903U CN 204202471 U CN204202471 U CN 204202471U
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- China
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- cooling tower
- pole plate
- droplet
- absorption pole
- retracting device
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Abstract
Cooling tower droplet retracting device belongs to energy-conserving and environment-protective technical field, relates to a kind of cooling tower droplet retracting device.The cooling tower droplet retracting device that the utility model provides a kind of droplet recovering effect good.The utility model comprises absorption pole frame and discharge electrode frame, discharge plume is connected with between its structural feature discharge electrode frame both sides, connect between absorption frame both sides, pole and absorption pole plate is set, absorption pole plate parallel vertical is arranged, and it is middle and parallel with absorption pole plate that discharge plume is arranged on adjacent two absorption pole plates.
Description
Technical field
The utility model belongs to energy-conserving and environment-protective technical field, relates to a kind of cooling tower droplet retracting device.
Background technology
The vaporific supersaturated air of current cooling tower discharge, suspension liquid droplet belongs to two-phase flow body.According to two-phase flow bulk properties, the particle diameter of water vapour droplet is 6-8 micron, calm just suspension.So the not sedimentation under air flow condition of the droplet of cooling tower, volatile quantity Q=0.0014 × temperature difference × model water yield=(1000 tons of boiler cooling towers) 3-4 ten thousand stere water=420-560 ton time, waste great lot of water resources.Recirculated water volatilizees, and residual chlorine ion accumulation exceeds standard, and becomes sewage, must discharge, and causes the pollution of natural environment.
Vaporific steam can only be discharged at present, there is no the equipment that droplet can be reclaimed.
Summary of the invention
The utility model is exactly for the problems referred to above, provides the cooling tower droplet retracting device that a kind of droplet recovering effect is good.
For achieving the above object, the utility model adopts following technical scheme, the utility model comprises absorption pole frame and discharge electrode frame, discharge plume is connected with between its structural feature discharge electrode frame both sides, absorption pole frame connects absorption pole plate is set, absorption pole plate parallel vertical is arranged, and it is middle and parallel with absorption pole plate that discharge plume is arranged on adjacent two absorption pole plates.
As a kind of preferred version, absorption pole plate described in the utility model and discharge plume are multiple, and absorption pole plate and discharge plume are staggered in the horizontal direction equidistantly to be arranged.
As another kind of preferred version, discharge electrode frame described in the utility model comprises transverse steel wire rope, vertical rod assembly and horizontal straight tube, often arranging described absorption pole plate divides the horizontal equidistant arrangement of absorption pole plate to form by polylith, absorption pole plate upper end is divided to be connected with transverse steel wire rope by vertical rod assembly, divide absorption pole plate lower end to be connected with horizontal straight tube by vertical rod assembly, transverse steel wire rope two ends, horizontal straight tube two ends all export with cooling tower and are connected; Often arrange described discharge plume to be made up of the longitudinal equidistant arrangement of many points of discharge plumes, point discharge plume floor projection with divide that to adsorb pole plate floor projection crossing.
As another kind of preferred version, vertical rod assembly described in the utility model adopts adjustable length vertical rod assembly.
As another kind of preferred version, discharge electrode frame described in the utility model comprises the upper discharge electrode round tube frame that be arranged in parallel and transfers electrode circle pipe support, upper discharge electrode round tube frame with transfer electrode circle pipe support and be connected by vertical plate, described discharge plume two ends are connected with vertical plate.
As another kind of preferred version, discharge electrode frame upper end described in the utility model is connected with vertical porcelain insulator, and porcelain vase lifting is fixed on porcelain vase seat, and porcelain vase seat is fixed on cooling tower steel reinforced concrete wall, and porcelain vase upper end is provided with rain cover.
As another kind of preferred version, rain cover described in the utility model adopts downward opening Plastic Drum.
As another kind of preferred version, between the adjacent described transverse steel wire rope of the utility model, be all connected with lateral isolation limiting bracket between horizontal straight tube, transverse steel wire rope both sides are provided with turnbuckle.
Secondly, be provided with medial surface from the bottom to top to the deflector of middle bent below horizontal straight tube two ends described in the utility model, deflector outer end and cooling tower export fixing; Deflector Inner end is placed in described porcelain vase side in cooling tower export center.
In addition, the spacing of adjacent described transverse steel wire rope described in the utility model is 400mm ~ 600mm, and transverse steel wire rope two ends fix non-return through cooling tower outlet armored concrete by baffle plate; Described steel wire rope adopts anticorrosion steel wire rope.
The utility model beneficial effect.
The utility model discharge plume forms form physics electric field arrangement with absorption pole plate, droplet particle positive electron on lotus in flowing is made with electrostatic field, adsorbed by absorption pole, whole electric charge is laid down in contact, become a part for absorption pole, absorption is continued to the positively charged droplet of follow-up follow-up, reaches and converge droplet and become the drop that particle diameter increases hundred times, to return in the air of flowing not settling flux.
Due to the water reclaiming normal temperature, circulation fluid total amount is substantially constant, and the accumulation of chlorion total amount seldom, decreases sewage discharge in recirculated water, reduces the operating cost of cooling tower.
In addition, the utility model can be arranged on cooling tower outlet top, namely not affect air flowing, the water of recovery again recyclable enter in recirculated water; And enter in air to cool to close to normal temperature, so do not affect gas, hydrothermal exchange due to water, gas.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described further.The utility model protection domain is not only confined to the statement of following content.
Fig. 1 is the utility model structural representation.
Fig. 2 is the utility model side view.
Fig. 3 is the utility model absorption electrode plate structure schematic diagram.
In figure, 1 for absorption pole plate, 2 discharge plumes, 3 for vertical rod assembly, 4 be steel wire rope, 5 for straight tube, 6 for limiting bracket, 7 for discharge electrode frame, 8 for porcelain vase, 9 for porcelain vase seat, 10 for rain cover, 11 for deflector, 12 be U-shaped bonding jumper.
Detailed description of the invention
As shown in the figure, the utility model comprises absorption pole frame and discharge electrode frame, discharge plume is connected with between its structural feature discharge electrode frame both sides, absorption pole frame connects absorption pole plate is set, absorption pole plate parallel vertical is arranged, and it is middle and parallel with absorption pole plate that discharge plume is arranged on adjacent two absorption pole plates.
Described absorption pole plate and discharge plume are multiple, and absorption pole plate and discharge plume are staggered in the horizontal direction equidistantly to be arranged.
Described discharge electrode frame comprises transverse steel wire rope, vertical rod assembly and horizontal straight tube, often arranging described absorption pole plate divides the horizontal equidistant arrangement of absorption pole plate to form by polylith, absorption pole plate upper end is divided to be connected with transverse steel wire rope by vertical rod assembly, divide absorption pole plate lower end to be connected with horizontal straight tube by vertical rod assembly, transverse steel wire rope two ends, horizontal straight tube two ends all export with cooling tower and are connected; Often arrange described discharge plume to be made up of the longitudinal equidistant arrangement of many points of discharge plumes, point discharge plume floor projection with divide that to adsorb pole plate floor projection crossing.
Described vertical rod assembly adopts adjustable length vertical rod assembly; Be convenient to the position adjusting absorption pole plate.
Described discharge electrode frame comprises the upper discharge electrode round tube frame that be arranged in parallel and transfers electrode circle pipe support, upper discharge electrode round tube frame with transfer electrode circle pipe support and be connected by vertical plate, described discharge plume two ends are connected with vertical plate.
Described discharge electrode frame upper end is connected with vertical porcelain insulator, and porcelain vase lifting is fixed on porcelain vase seat, and porcelain vase seat is fixed on cooling tower steel reinforced concrete wall, and porcelain vase upper end is provided with rain cover.
Described rain cover adopts downward opening Plastic Drum; Prevent contacting rain water porcelain vase.
Between adjacent described transverse steel wire rope, be all connected with lateral isolation limiting bracket between horizontal straight tube, transverse steel wire rope both sides are provided with turnbuckle.
Be provided with medial surface from the bottom to top to the deflector of middle bent below described horizontal straight tube two ends, deflector outer end and cooling tower export fixing; Deflector Inner end is placed in described porcelain vase side in cooling tower export center.Arranging deflector makes ascending air not contact porcelain vase.
The spacing of described adjacent described transverse steel wire rope is 400mm ~ 600mm, and transverse steel wire rope two ends fix non-return through cooling tower outlet armored concrete by baffle plate; Described steel wire rope adopts anticorrosion steel wire rope.
Described vertical plate can adopt 10 millimeters of plates.
Described discharge plume is circle line or Saw blade.
Described absorption pole plate is corrosion resistant plate or graphite cake.
Each parts can adopt stainless steel or metalwork surface to do preservative treatment.
Discharge plume outside absorption pole plate is provided with turnbuckle.
Described porcelain vase is multiple, and each porcelain vase is arranged in parallel.
The vertical range of described deflector upper end and discharge electrode frame lower end is 600mm.
The voltage of described discharge plume can be set to 50-72KV, current squaring rice=1-0.5mA.
Described point of absorption pole plate upper and lower side is all connected with vertical rod assembly by inlaying U-shaped bonding jumper.
Simulated experiment; Medium=air adds water atomizing spray--close to normal-temperature water steam, electrostatic field is energized---outlet water white transparency.
Electrostatic field power-off---outlet spray water steam.
Industrial experiment; High-temperature flue gas shower water, becomes vaporific flue gas, and cross electrostatic field, droplet is recovered, purer CO
2gas discharges.
Below in conjunction with accompanying drawing, the course of work of the present utility model is described.
Droplet is to absorption pole plate place, and droplet is adsorbed pole plate absorption, the vertical out-fall of residue saturated air--enter air without the transparent air of colour saturation.
The droplet adsorbed enters tower Inner eycle liquid converge vertical current on absorption pole plate under.
According to the cooling tower volatilization water formula=0.0014 × flow × temperature difference=0.0014 × 30000 × 10=420 ton.
Air enters from tower bottom; Air humidity 80%, discharged air humidity 100%, has 20% gasified water discharge.
So volatilization vaporous water=20% that volatilization water=air total amount is carried secretly, receive 80%.
Because volatilization water reduces, relative complement water-filling reduces, and relative halogen ion reduces, and sewer reduces, and supplementing water reduces, and reaches water saving object; Be more suitable for water-deficient area.
Volatilization water consumption is with droplet form--supersaturation droplet, droplet in high-energy physics electrostatic field on 100% lotus+electronics, 100% is adsorbed by absorption pole, droplet absorption after electric discharge, on lotus with pole plate electronics of the same race, absorption affinity disappear, absorption droplet continuous adsorption, converge, increase to stream, along under pole plate vertical current, size droplet diameter reaches several millimeters, be the hundred times of mist droplet particle size, air flowing can not make it suspend, and vertical sedimentation enters the circulatory pool in cooling tower.
Be understandable that, above about specific descriptions of the present utility model, the technical scheme described by the utility model embodiment is only not limited to for illustration of the utility model, those of ordinary skill in the art is to be understood that, still can modify to the utility model or equivalent replacement, to reach identical technique effect; Needs are used, all within protection domain of the present utility model as long as meet.
Claims (10)
1.
cooling tower droplet retracting device, comprise absorption pole frame and discharge electrode frame, it is characterized in that being connected with discharge plume between discharge electrode frame both sides, absorption pole frame connects absorption pole plate is set, absorption pole plate parallel vertical is arranged, and it is middle and parallel with absorption pole plate that discharge plume is arranged on adjacent two absorption pole plates.
2.
according to claim 1, cooling tower droplet retracting device, is characterized in that described absorption pole plate and discharge plume are multiple, and absorption pole plate and discharge plume are staggered in the horizontal direction equidistantly to be arranged.
3.
cooling tower droplet retracting device according to claim 1, it is characterized in that described discharge electrode frame comprises transverse steel wire rope, vertical rod assembly and horizontal straight tube, often arranging described absorption pole plate divides the horizontal equidistant arrangement of absorption pole plate to form by polylith, absorption pole plate upper end is divided to be connected with transverse steel wire rope by vertical rod assembly, divide absorption pole plate lower end to be connected with horizontal straight tube by vertical rod assembly, transverse steel wire rope two ends, horizontal straight tube two ends all export with cooling tower and are connected; Often arrange described discharge plume to be made up of the longitudinal equidistant arrangement of many points of discharge plumes, point discharge plume floor projection with divide that to adsorb pole plate floor projection crossing.
4.
according to claim 3, cooling tower droplet retracting device, is characterized in that described vertical rod assembly adopts adjustable length vertical rod assembly.
5.
cooling tower droplet retracting device according to claim 1, it is characterized in that described discharge electrode frame comprises the upper discharge electrode round tube frame that be arranged in parallel and transfers electrode circle pipe support, upper discharge electrode round tube frame with transfer electrode circle pipe support and be connected by vertical plate, described discharge plume two ends are connected with vertical plate.
6.
according to claim 3, cooling tower droplet retracting device, is characterized in that described discharge electrode frame upper end is connected with vertical porcelain insulator, and porcelain vase lifting is fixed on porcelain vase seat, and porcelain vase seat is fixed on cooling tower steel reinforced concrete wall, and porcelain vase upper end is provided with rain cover.
7.
according to claim 6, cooling tower droplet retracting device, is characterized in that described rain cover adopts downward opening Plastic Drum.
8.
according to claim 3, cooling tower droplet retracting device, it is characterized in that between adjacent described transverse steel wire rope, be all connected with lateral isolation limiting bracket between horizontal straight tube, transverse steel wire rope both sides are provided with turnbuckle.
9.
according to claim 6, cooling tower droplet retracting device, is characterized in that being provided with medial surface from the bottom to top to the deflector of middle bent below described horizontal straight tube two ends, and deflector outer end and cooling tower export fixing; Deflector Inner end is placed in described porcelain vase side in cooling tower export center.
10.
according to claim 3, cooling tower droplet retracting device, is characterized in that the spacing of described adjacent described transverse steel wire rope is 400mm ~ 600mm, and transverse steel wire rope two ends fix non-return through cooling tower outlet armored concrete by baffle plate; Described steel wire rope adopts anticorrosion steel wire rope.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420550903.2U CN204202471U (en) | 2014-09-24 | 2014-09-24 | Cooling tower droplet retracting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420550903.2U CN204202471U (en) | 2014-09-24 | 2014-09-24 | Cooling tower droplet retracting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204202471U true CN204202471U (en) | 2015-03-11 |
Family
ID=52660418
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420550903.2U Expired - Fee Related CN204202471U (en) | 2014-09-24 | 2014-09-24 | Cooling tower droplet retracting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204202471U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104251642A (en) * | 2014-09-24 | 2014-12-31 | 姜桂英 | Water cooling tower fogdrop recovery device |
| CN110030869A (en) * | 2019-05-20 | 2019-07-19 | 广东览讯科技开发有限公司 | High-pressure electrostatic inhales floating water collector in a kind of cooling stack |
-
2014
- 2014-09-24 CN CN201420550903.2U patent/CN204202471U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104251642A (en) * | 2014-09-24 | 2014-12-31 | 姜桂英 | Water cooling tower fogdrop recovery device |
| CN110030869A (en) * | 2019-05-20 | 2019-07-19 | 广东览讯科技开发有限公司 | High-pressure electrostatic inhales floating water collector in a kind of cooling stack |
| CN110030869B (en) * | 2019-05-20 | 2024-02-02 | 广东览讯科技开发有限公司 | High-voltage electrostatic flotation water absorbing device in natural ventilation cooling tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20150311 Termination date: 20170924 |