CN201815237U - Pneumatic emulsifying desulfurizing tower - Google Patents
Pneumatic emulsifying desulfurizing tower Download PDFInfo
- Publication number
- CN201815237U CN201815237U CN2010205718260U CN201020571826U CN201815237U CN 201815237 U CN201815237 U CN 201815237U CN 2010205718260 U CN2010205718260 U CN 2010205718260U CN 201020571826 U CN201020571826 U CN 201020571826U CN 201815237 U CN201815237 U CN 201815237U
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- tower
- gas
- desulfurizing tower
- pneumatic emulsifying
- liquid
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Abstract
The utility model provides a pneumatic emulsifying desulfurizing tower, which comprises a tower body, a defogger, a stirring machine, an alkali supplementing pipe, a water replenishing pipe, a wind inlet pipe, a liquid-collecting tank, a plurality of circulation fluid distributing pipes, a circulation pump and a solenoid valve, wherein one end of the circulation pump is connected with the liquid-collecting tank, while the other end is connected with the solenoid valve and the circulation fluid distributing pipes; a gas inlet chamber, a wind energy collecting cyclone chamber and a gas-liquid separation chamber are arranged in the tower; a cyclone generator is mounted under the wind energy collecting cyclone chamber; and two groups of plane dehydrating plate groups are distributed in a V shape in the gas-liquid separation chamber and arranged in the horizontal direction in an opposite way. The pneumatic emulsifying desulfurizing tower not only reduces the manufacturing cost, but also remarkably increases the dehydrating effect because the areas of the dehydrating plates and the contact probability with air are increased, thereby enhancing the desulfurizing effect of the pneumatic emulsifying desulfurizing tower.
Description
Technical field
The utility model relates to a kind of Pneumatic emulsifying desulfurizing tower.
Background technology
Existing Pneumatic emulsifying desulfurizing tower comprises that tower body, demister, mixer, benefit alkali pipe, filling pipe, blast pipe, collecting tank, many circulation fluid liquid distributors, circulating pump, magnetic valve, circulating pump one ends link to each other with collecting tank, and its other end links to each other with many circulation fluid liquid distributors with magnetic valve.Be provided with inlet plenum, wind-force energy-collecting cyclonic chamber, gas-liquid separation chamber in the tower body, the cyclone generator is equipped with in wind-force energy-collecting cyclonic chamber below, and there is the multifoil shoe of one group of arc-shaped curved surface in described gas-liquid separation chamber.Because not only manufacture difficulty is bigger for the dewatering plate of arc-shaped curved surface, cost is higher, and dehydrating effect is undesirable, makes desulfurized effect be affected.
Summary of the invention
The purpose of this utility model is to overcome shortcoming of the prior art, and a kind of simple in structure, high efficiency, Pneumatic emulsifying desulfurizing tower cheaply are provided.
The purpose of this utility model is to be achieved by following technical proposals:
Pneumatic emulsifying desulfurizing tower of the present utility model comprises that tower body, demister, mixer, benefit alkali pipe, filling pipe, blast pipe, collecting tank, many circulation fluid liquid distributors, circulating pump, magnetic valve, circulating pump one ends link to each other with collecting tank, its other end links to each other with many circulation fluid liquid distributors with magnetic valve, be provided with inlet plenum, wind-force energy-collecting cyclonic chamber, gas-liquid separation chamber in the tower body, the cyclone generator is equipped with in wind-force energy-collecting cyclonic chamber below, there is the plane multifoil shoe by two groups of V-shaped distributions in described gas-liquid separation chamber, and two groups of multifoil shoe become relative arrangement in the horizontal direction.
Described cyclone generator is made up of 4 to 80 blades, is 1 to 3 layer, radial arrangement, and every blade and horizontal sextant angle are 8 to 78 degree, the height of cyclone generator is 50 millimeters to 2000 millimeters.
Owing to adopted said structure, make Pneumatic emulsifying desulfurizing tower of the present utility model not only manufacturing cost reduce, and because the area of dewatering plate and increase with the contact probability of gas, dehydrating effect obviously increases, thereby the desulfurized effect of Pneumatic emulsifying desulfurizing tower is enhanced.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structure vertical view of cyclone generator of the present utility model.
The specific embodiment
The utility model will be further described below in conjunction with accompanying drawing.
In Fig. 1 and Fig. 2, tubular tower body 1 is by the steel plate manufacturing, and its lower end is provided with a collecting tank 11, and its underpart is provided with inlet plenum 2, and its middle part is provided with wind-force energy-collecting cyclonic chamber 3, and its top is provided with gas-liquid separation chamber 4, and its upper end is provided with gas outlet 12.Under these collecting tank 11 liquid levels agitator 7 and blast pipe 10 are housed, collecting tank 11 can be located at outside the tower body 1.This inlet plenum 2 has an air inlet 14, and there are the alkali pipe 8 of benefit and filling pipe 9 in its top.Cyclone generator 5 is arranged at these wind-force energy-collecting cyclonic chamber 3 bottoms, and its top is provided with many circulation fluid liquid distributors 13.This cyclone generator 5 is made up of 4 to 80 corrugated blades, blade 18 be 1 to 3 layer radially irregular alignment arrange that every blade and horizontal sextant angle are 8 to 78 to spend.Blade 18 metallic plate manufacturing, its external diameter are fixed on tower body 1 inwall, and its internal diameter is fixed on center steel pipe 19 outer walls.The height of cyclone generator 5 is 50 to 2000 millimeters.It is to quicken energy collecting, and quickens, turns to according to predefined angle, forms the spiral air flow with suitable energy and holds and shred circulation fluid, forms the device of cyclone gas-liquid layer.
This gas-liquid separation chamber 4 has one group of 6 and 6 ', two groups of multifoil shoe of plane multifoil shoe by two groups of V-shaped distributions by steel plate manufacturing angle bar structure to become relative arrangement in the horizontal direction.Because the area of dewatering plate and increase with the contact probability of gas, dehydrating effect obviously increases, thereby the desulfurized effect of Pneumatic emulsifying desulfurizing tower is enhanced.And manufacturing cost of the present utility model is reduced.Circulating pump 15 entrance points link to each other with collecting tank 11, and its port of export links to each other with magnetic valve 16, many circulation fluid liquid distributors 13 respectively and densimeter and pH value sensor are housed.Filling pipe 9 links to each other with the outer running water pipe of tower.Mending alkali pipe 8 links to each other with the outer alkali lye pond of tower.
During work, flue gas enters inlet plenum 2 by smoke inlet 14 under the air-introduced machine effect outside tower, be recycled the circulation fluid humidifying that 13 ejections of liquid liquid distributor fall through inlet plenum top and enter wind-force energy-collecting cyclonic chamber 3, under the air-introduced machine effect of the flue gas of humidifying outside tower body 1, has certain wind-force kinetic energy, flue gas is quickened energy collecting by the cyclone generator 5 of wind-force energy-collecting cyclonic chamber 3, flow velocity improves 3 times and break-in, quicken by predefined angle, turn to, formation has the spiral air flow rising of suitable energy and holds and shred from the free-falling circulation desulfurization liquid of top circulation fluid liquid distributor 13 ejections, make this liquid be full of trickle bubble, form stable cyclone gas-liquid layer, a large amount of trickle bubbles and the drop that is cut into nano sized particles are arranged in the layer, carry out SO in the strong mass transfer flue gas between gas-liquid
2Being recycled drop with particulate thoroughly absorbs and chemical reaction.Remove SO
2Rise to gas-liquid separation chamber 4 by multifoil shoe 6 and 6 ' dehydration with the flue gas of particulate, discharge outside the tower body through exporting 12, part drop band the SO that absorbs
2Drop to collecting tank 11 with particulate, become circulation fluid, the flue gas that enters through inlet plenum 2 humidifyings in the dropping process.If circulation fluid contains solid or sulfide, the air oxidation that needs agitator 7 stirrings and enter by blast pipe 10, making sulfite oxidation is the sulphate crystal body, when circulation fluid reaches finite concentration, the part circulation fluid be recycled pump 15 extract out through magnetic valve 16 discharge, dehydration, dry, become the desulfuration byproduct that economic worth is arranged.Collecting tank 11 is provided with liquid level gauge, and filling pipe 9 water inlets replenished when liquid level descended, and guaranteed the liquid level of collecting tank 11, replenishes desulfurizing agent by mending alkali pipe 8 when circulating pump 15 outlets have densimeter and pH value sensor, pH value to be lower than setting value.Desulfurizing agent is limewash, agstone emulsion, other alkaline aqueous solutions of calcium carbide mud.
Claims (2)
1. Pneumatic emulsifying desulfurizing tower, comprise that tower body, demister, mixer, benefit alkali pipe, filling pipe, blast pipe, collecting tank, many circulation fluid liquid distributors, circulating pump, magnetic valve, circulating pump one ends link to each other with collecting tank, its other end links to each other with many circulation fluid liquid distributors with magnetic valve, be provided with inlet plenum, wind-force energy-collecting cyclonic chamber, gas-liquid separation chamber in the tower body, the cyclone generator is equipped with in wind-force energy-collecting cyclonic chamber below, it is characterized in that, there is the plane multifoil shoe by two groups of V-shaped distributions in described gas-liquid separation chamber, and two groups of multifoil shoe become relative arrangement in the horizontal direction.
2. according to the Pneumatic emulsifying desulfurizing tower of claim 1, it is characterized in that described cyclone generator is made up of 4 to 80 blades, is 1 to 3 layer, radial arrangement, and every blade and horizontal sextant angle are 8 to 78 degree, the height of cyclone generator is 50 millimeters to 2000 millimeters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205718260U CN201815237U (en) | 2010-10-22 | 2010-10-22 | Pneumatic emulsifying desulfurizing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205718260U CN201815237U (en) | 2010-10-22 | 2010-10-22 | Pneumatic emulsifying desulfurizing tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201815237U true CN201815237U (en) | 2011-05-04 |
Family
ID=43913209
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205718260U Expired - Lifetime CN201815237U (en) | 2010-10-22 | 2010-10-22 | Pneumatic emulsifying desulfurizing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201815237U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104162356A (en) * | 2014-08-27 | 2014-11-26 | 邹海明 | Double-multitube integrated type pneumatic emulsification desulfurizing tower |
| CN108220586A (en) * | 2017-12-28 | 2018-06-29 | 郴州雄风环保科技有限公司 | Noble metal technique is extracted from high-sulfur palladium platinum waste material |
| CN109276953A (en) * | 2017-07-21 | 2019-01-29 | 德梅斯特(上海)环保科技有限公司 | A kind of dedusting demister and dedusting demister system |
| CN111229036A (en) * | 2020-01-20 | 2020-06-05 | 宁波大学 | Ship exhaust gas desulfurization device |
-
2010
- 2010-10-22 CN CN2010205718260U patent/CN201815237U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104162356A (en) * | 2014-08-27 | 2014-11-26 | 邹海明 | Double-multitube integrated type pneumatic emulsification desulfurizing tower |
| CN104162356B (en) * | 2014-08-27 | 2016-08-17 | 邹海明 | A kind of double multitube combined Pneumatic emulsifying desulfurizing tower |
| CN109276953A (en) * | 2017-07-21 | 2019-01-29 | 德梅斯特(上海)环保科技有限公司 | A kind of dedusting demister and dedusting demister system |
| CN108220586A (en) * | 2017-12-28 | 2018-06-29 | 郴州雄风环保科技有限公司 | Noble metal technique is extracted from high-sulfur palladium platinum waste material |
| CN111229036A (en) * | 2020-01-20 | 2020-06-05 | 宁波大学 | Ship exhaust gas desulfurization device |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110504 |
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| CX01 | Expiry of patent term |