CN203355524U - Spray tower - Google Patents
Spray tower Download PDFInfo
- Publication number
- CN203355524U CN203355524U CN 201320308194 CN201320308194U CN203355524U CN 203355524 U CN203355524 U CN 203355524U CN 201320308194 CN201320308194 CN 201320308194 CN 201320308194 U CN201320308194 U CN 201320308194U CN 203355524 U CN203355524 U CN 203355524U
- Authority
- CN
- China
- Prior art keywords
- tower body
- liquid
- eddy flow
- liquid distribution
- tower
- 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
- 239000007921 spray Substances 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 244000144985 peep Species 0.000 claims description 4
- 239000000463 material Substances 0.000 abstract description 6
- 238000000746 purification Methods 0.000 abstract description 6
- 239000002912 waste gas Substances 0.000 abstract description 4
- 239000000428 dust Substances 0.000 abstract description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 2
- 239000003546 flue gas Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000003500 flue dust Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model relates to the field of waste gas purification and provides a spray tower. The spray tower comprises a tower body and a tower body support frame, wherein an air inlet is formed in the tower body; a plurality layers of swirl liquid distribution boards are uniformly distributed above the air inlet; a liquid distribution device is arranged above the swirl liquid distribution boards; a swirl liquid removing board is arranged above the liquid distribution device; a liquid baffle ring is arranged between the swirl liquid removing board and the exhaust outlet in the top of the tower body; a plurality of observation holes are formed in the tower body. The spray tower has the advantages of large mass transfer area, high efficiency, small size, easiness in processing, economy of material, convenience in operation, and the like. The spray tower can be used for treating dust-containing flue gas.
Description
Technical field
The utility model relates to the waste gas purification field, is specifically related to a kind of spray column, for the purification to materials such as fine dust, smog, steams.
Background technology
Waste gas purification mainly refers to the work of being administered for industrial waste gas such as dust granules thing, flue gas flue dust, gas with foreign flavor, the toxic and harmful of industrial site generation.Exhaust gas purifying method is divided into dilution diffusion method and water absorption method etc.Its expense of equipment requirement for waste gas purification is low, power consumption less, non-secondary pollution, accomplish to save energy consumption as far as possible, environmental.
Summary of the invention
The advantages such as the purpose of this utility model is exactly, in order to overcome above-mentioned the deficiencies in the prior art part, to provide a kind of spray column, has a mass transfer area large, and efficiency is high, and volume is little, and processing is simple, saves material, easy to operate, can be used for processing ash-laden gas.
The purpose of this utility model is achieved by the following technical measures: a kind of spray column, comprise tower body and tower body bracing frame, described tower body is provided with air inlet, the air inlet top is evenly equipped with some layers of eddy flow liquid distribution plate, eddy flow liquid distribution plate top is provided with liquid distributor, the liquid distributor top is provided with the eddy flow liquid-removing plate, between the exhaust outlet at eddy flow liquid-removing plate and tower body top, is provided with flinger ring, and tower body is provided with some peep holes.
In technique scheme, described tower body bottom is provided with reservoir, and reservoir is communicated with the water inlet pipe of liquid distributor through water circulating pump.
The utility model spray column is simple in structure, and operability large (superficial linear velocity in a column 0.5-3m/s) is difficult for stopping up, and mass transfer area is large, and efficiency is high, and volume is little, and processing is simple, saves material, easy to operate, can be used for processing ash-laden gas etc.The utility model safeguards without the professional, easy to usely through on-the-spot guidance, gets final product operation and maintenance, and general purification efficiency can reach 90%.
The accompanying drawing explanation
The structural representation that Fig. 1 is the utility model spray column.
Wherein: 1. tower body, 2. flinger ring, 3. eddy flow liquid-removing plate, 4. water inlet pipe, 5. liquid distributor, 6. eddy flow liquid distribution plate, 7. air inlet, 8. tower body bracing frame, 9. peep hole, 10. reservoir, 11. water circulating pumps.
The specific embodiment
Below in conjunction with drawings and Examples, the utility model will be further described.
As shown in Figure 1, the present embodiment provides a kind of spray column, comprise tower body 1 and tower body bracing frame 8, described tower body 1 is provided with air inlet 7, air inlet 7 tops are evenly equipped with some layers of eddy flow liquid distribution plate 6, and eddy flow liquid distribution plate 6 tops are provided with liquid distributor 5, and liquid distributor 5 tops are provided with eddy flow liquid-removing plate 3, be provided with flinger ring 2 between the exhaust outlet at eddy flow liquid-removing plate 3 and tower body 1 top, tower body 1 is provided with some peep holes 9.Described tower body 1 bottom is provided with reservoir 10, and reservoir 10 is communicated with the water inlet pipe 4 of liquid distributor 5 through water circulating pump 11.
In the above-described embodiments, described eddy flow liquid distribution plate utilizes the effect of spiral board guiding, and uniform wind-force makes band dirt air-flow uniform, and the motion of fixed-direction is arranged.Utilization allows gas-liquid fully contact with the motion of dirt air-flow, wants less by 60% than other equipment resistance of the same type.
In the above-described embodiments, during the work of described liquid distributor, inside has certain pressure (0.5MPa), by spout, sprays water smoke, allow with the dirt air-flow in the liquid mist by reaching the effect of dedusting.
In the above-described embodiments, the eddy flow liquid distribution plate is mainly to allow air-flow to central rotation, reaches the effect of gather qi together, and the eddy flow liquid-removing plate is mainly to allow air-flow to the rotation of tower wall, reaches the effect of the liquid that dewaters.
When the present embodiment is used, that by exhaust system, is drawn contains flue dust material air-flow, from the sidepiece air inlet 7 of spray column, enters, and air-flow is from bottom to top one by one through eddy flow liquid distribution plate 6 layer by layer, after crossing 3 demists of eddy flow liquid-removing plate, from top vent, enter atmosphere.Absorption liquid is recycled water pump 11 sucking-offs from reservoir 10, enter the last layer eddy flow liquid distribution plate 6 of tower through liquid distributor 5, its liquid flow direction is vertical with airflow direction, and in tower, neutralization absorbs the flue dust material, from top to bottom finally by overfall, enter in reservoir 10, recycle.
Claims (2)
1. a spray column, comprise tower body and tower body bracing frame, it is characterized in that: described tower body is provided with air inlet, the air inlet top is evenly equipped with some layers of eddy flow liquid distribution plate, eddy flow liquid distribution plate top is provided with liquid distributor, the liquid distributor top is provided with the eddy flow liquid-removing plate, between the exhaust outlet at eddy flow liquid-removing plate and tower body top, is provided with flinger ring, and tower body is provided with some peep holes.
2. spray column according to claim 1, it is characterized in that: described tower body bottom is provided with reservoir, and reservoir is communicated with the water inlet pipe of liquid distributor through water circulating pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320308194 CN203355524U (en) | 2013-05-31 | 2013-05-31 | Spray tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320308194 CN203355524U (en) | 2013-05-31 | 2013-05-31 | Spray tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203355524U true CN203355524U (en) | 2013-12-25 |
Family
ID=49803349
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320308194 Expired - Fee Related CN203355524U (en) | 2013-05-31 | 2013-05-31 | Spray tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203355524U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105381669A (en) * | 2015-11-27 | 2016-03-09 | 新乡学院 | High temperature tail gas deduster |
| CN105854472A (en) * | 2016-05-19 | 2016-08-17 | 沈建南 | Haze removing device for indoor air purification |
| CN106731355A (en) * | 2017-02-07 | 2017-05-31 | 曹小高 | Full-automatic tobacco gas separates and recovers integration apparatus |
-
2013
- 2013-05-31 CN CN 201320308194 patent/CN203355524U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105381669A (en) * | 2015-11-27 | 2016-03-09 | 新乡学院 | High temperature tail gas deduster |
| CN105854472A (en) * | 2016-05-19 | 2016-08-17 | 沈建南 | Haze removing device for indoor air purification |
| CN106731355A (en) * | 2017-02-07 | 2017-05-31 | 曹小高 | Full-automatic tobacco gas separates and recovers integration apparatus |
| CN106731355B (en) * | 2017-02-07 | 2019-04-16 | 曹小高 | Full-automatic flue gas separates and recovers integration apparatus |
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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: 20131225 Termination date: 20140531 |