CN205965492U - Desulfurizing tower - Google Patents
Desulfurizing tower Download PDFInfo
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- CN205965492U CN205965492U CN201620956748.3U CN201620956748U CN205965492U CN 205965492 U CN205965492 U CN 205965492U CN 201620956748 U CN201620956748 U CN 201620956748U CN 205965492 U CN205965492 U CN 205965492U
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- air flow
- desulfurizing tower
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Abstract
An object of the utility model is to provide a desulfurizing tower, including desulfurizing tower, desulfurizing tower lower part one side is provided with the flue gas entry, and the top is provided with the exhanst gas outlet, and the bottom is provided with the thick liquid pond, and thick liquid pond one side is provided with the liquid outlet, desulfurizing tower inside from upward install an air flow distribution layer, the 2nd air flow distribution layer downwards in proper order, spray the layer it has a plurality of slant gas flow tube to become round annular arrangement on an air flow distribution layer, the 2nd air flow distribution layer, and this desulfurizing tower simple structure, desulfurization effect is good, operation expense is low.
Description
Technical field
This utility model belongs to desulfuration field, more particularly, to a kind of desulfurizing tower.
Background technology
Sulfur dioxide is to cause one of main matter of air pollution, very big to human health damage.China is by dioxy
Change sulfur and be classified as a kind of main regulatory control air pollutants, and using the concentration level of Sulfur Dioxide In The Atmosphere as evaluation air
One important indicator of quality, the sulfur dioxide 80~90% in air derives from industrial pollution discharge, so desulfurizing tower is as work
Visual plant in industry flue gas desulphurization system, applies widely, but existing desulfurizing tower desulfurized effect can not be expired completely
How toe ring guaranteed request, so improve the problem that desulfurizing tower desulfuration efficiency is affiliated industry technology personnel extremely concern.
Content of the invention
The purpose of this utility model is to provide a kind of desulfurizing tower, and this Structure of Flue Gas Desulfuration Absorbing is simple, desulfurized effect is good, run dimension
Shield low cost.
For achieving the above object, the technical solution of the utility model is:A kind of desulfurizing tower, including desulfurizing tower, described desulfurization
Tower bottom side is provided with smoke inlet, and top is provided with exhanst gas outlet, and bottom is provided with slurry pool, and slurry pool side is provided with
Liquid outlet, is from up to down sequentially installed with the first air flow method layer, the second air flow method layer, spraying layer inside described desulfurizing tower,
It is provided with spray head, edge is provided with spraying layer leakage fluid dram, described first air flow method layer, the second air flow method in the middle part of spraying layer
Become circular on layer and be disposed with some oblique gas flow tube, edge is provided with the first air flow method layer leakage fluid dram, the second air flow method
Layer leakage fluid dram, some oblique gas flow tube outgassing direction on described first air flow method layer is arranged in the direction of the clock, the second gas
Some oblique gas flow tube outgassing direction on flow point layer of cloth is arranged counterclockwise.
Described oblique gas flow tube is 35~55 degree with the angle of place air flow method layer.
This utility model structure is simple, and easy to use, desulfurized effect is good, is provided with two air flow method layers, air flow method
Become circular on layer and be disposed with some oblique gas flow tube, when flue gas passes through air flow method layer, the flue gas that oblique gas flow tube will rise
Form eddy flow, the oblique gas flow tube outgassing direction increasing on gas-liquid contact time, and two-layer air flow method layer is contrary, further
Increase gas-liquid contact time, thus improving desulfurized effect.
Brief description
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the first air flow method Rotating fields schematic diagram of the present utility model.
Specific embodiment
As shown in Figure 1, 2, a kind of desulfurizing tower, including desulfurizing tower 1, desulfurizing tower 1 bottom side is provided with smoke inlet 2, top
Portion is provided with exhanst gas outlet 3, and bottom is provided with slurry pool 4, and slurry pool 4 one side bottom is provided with liquid outlet 41, inside desulfurizing tower
From up to down it is sequentially installed with the first air flow method layer 5, the second air flow method layer 6, spraying layer 7, in the middle part of spraying layer 7, be provided with spray
Pouring 71, edge is provided with spraying layer leakage fluid dram 72, the first air flow method layer 5 becomes circular and is disposed with some oblique gas flow tube
8, oblique gas flow tube outgassing direction is arranged in the direction of the clock, and the angle of oblique gas flow tube 8 and the first air flow method layer is 45 degree,
First air flow method layer edge is provided with the first air flow method layer leakage fluid dram 51, and the second air flow method layer 6 becomes circular arrangement
There are some oblique gas flow tube, oblique gas flow tube outgassing direction is arranged in the direction of the clock, oblique gas flow tube and the second air flow method
The angle of layer is 45 degree, and the second air flow method layer edge is provided with the second air flow method layer leakage fluid dram 61.
It would be desirable to the flue gas of desulfurization is passed through desulfurizing tower from smoke inlet during use, flue gas rises through spray head, Ran Houjing
Cross the oblique gas flow tube on the second air flow method layer and form eddy flow counterclockwise, reach the first air flow method layer, and by the first air-flow
Oblique gas flow tube on distribution layer forms eddy flow clockwise, and change twice increased gas-liquid contact time, improves desulfurization degree, phase
Between produce liquid pass through the leakage fluid dram of each layer flow to slurry pool discharge.
Claims (2)
1. a kind of desulfurizing tower, including desulfurizing tower, described desulfurizing tower bottom side is provided with smoke inlet, and top is provided with flue gas and goes out
Mouthful, bottom is provided with slurry pool, and slurry pool side is provided with liquid outlet, is from up to down sequentially installed with the inside described desulfurizing tower
One air flow method layer, the second air flow method layer, spraying layer, are provided with spray head in the middle part of spraying layer, edge is provided with spraying layer row
Liquid mouth, described first air flow method layer, the second air flow method layer becomes circular and is disposed with some oblique gas flow tube, edge is arranged
There are the first air flow method layer leakage fluid dram, the second air flow method layer leakage fluid dram, some oblique gas on described first air flow method layer
Flow tube outgassing direction is arranged in the direction of the clock, and some oblique gas flow tube outgassing direction on the second air flow method layer is pressed counterclockwise
Direction is arranged.
2. desulfurizing tower according to claim 1 it is characterised in that:Described oblique gas flow tube and the folder of place air flow method layer
Angle is 35~55 degree.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620956748.3U CN205965492U (en) | 2016-08-29 | 2016-08-29 | Desulfurizing tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620956748.3U CN205965492U (en) | 2016-08-29 | 2016-08-29 | Desulfurizing tower |
Publications (1)
Publication Number | Publication Date |
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CN205965492U true CN205965492U (en) | 2017-02-22 |
Family
ID=58037639
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201620956748.3U Expired - Fee Related CN205965492U (en) | 2016-08-29 | 2016-08-29 | Desulfurizing tower |
Country Status (1)
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CN (1) | CN205965492U (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106914123A (en) * | 2017-03-30 | 2017-07-04 | 成都申川节能环保工程有限公司 | A kind of efficient desulfurizing tower |
CN107174886A (en) * | 2017-06-19 | 2017-09-19 | 王艺璁 | A kind of electric automatization dust arrester |
CN107213761A (en) * | 2017-06-30 | 2017-09-29 | 成都川通达科技有限公司 | A kind of Novel desulfurization tower |
CN107297134A (en) * | 2017-05-31 | 2017-10-27 | 泉州科维嘉电力有限公司 | A kind of smoke eliminator of high desulfurization efficiency |
CN107362632A (en) * | 2017-05-31 | 2017-11-21 | 泉州科维嘉电力有限公司 | A kind of energy-efficient sulfur-containing flue gas purifying system |
CN107456818A (en) * | 2017-06-19 | 2017-12-12 | 王艺璁 | A kind of automatic dust removing apparatus of high-efficient purification air |
CN114100332A (en) * | 2021-10-27 | 2022-03-01 | 中冶赛迪重庆信息技术有限公司 | Cyclone device of large-diameter tower body |
CN115090211A (en) * | 2022-06-08 | 2022-09-23 | 苏州思萃热控材料科技有限公司 | Drying and granulating integrated equipment for preparing aluminum silicon carbide composite material |
-
2016
- 2016-08-29 CN CN201620956748.3U patent/CN205965492U/en not_active Expired - Fee Related
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106914123A (en) * | 2017-03-30 | 2017-07-04 | 成都申川节能环保工程有限公司 | A kind of efficient desulfurizing tower |
CN107297134A (en) * | 2017-05-31 | 2017-10-27 | 泉州科维嘉电力有限公司 | A kind of smoke eliminator of high desulfurization efficiency |
CN107362632A (en) * | 2017-05-31 | 2017-11-21 | 泉州科维嘉电力有限公司 | A kind of energy-efficient sulfur-containing flue gas purifying system |
CN107297134B (en) * | 2017-05-31 | 2019-07-30 | 河北用邦环保设备科技有限公司 | A kind of flue gas purification device of high desulfurization efficiency |
CN107174886A (en) * | 2017-06-19 | 2017-09-19 | 王艺璁 | A kind of electric automatization dust arrester |
CN107456818A (en) * | 2017-06-19 | 2017-12-12 | 王艺璁 | A kind of automatic dust removing apparatus of high-efficient purification air |
CN107174886B (en) * | 2017-06-19 | 2018-09-11 | 王艺璁 | A kind of electric automatization dust-extraction unit |
CN107213761A (en) * | 2017-06-30 | 2017-09-29 | 成都川通达科技有限公司 | A kind of Novel desulfurization tower |
CN114100332A (en) * | 2021-10-27 | 2022-03-01 | 中冶赛迪重庆信息技术有限公司 | Cyclone device of large-diameter tower body |
CN115090211A (en) * | 2022-06-08 | 2022-09-23 | 苏州思萃热控材料科技有限公司 | Drying and granulating integrated equipment for preparing aluminum silicon carbide composite material |
CN115090211B (en) * | 2022-06-08 | 2023-09-22 | 苏州思萃热控材料科技有限公司 | Integrative equipment of stoving pelletization for preparation of aluminium carborundum combined material |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170222 Termination date: 20180829 |
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CF01 | Termination of patent right due to non-payment of annual fee |