CN102974193A - Tail gas absorbing tower - Google Patents
Tail gas absorbing tower Download PDFInfo
- Publication number
- CN102974193A CN102974193A CN2012105685947A CN201210568594A CN102974193A CN 102974193 A CN102974193 A CN 102974193A CN 2012105685947 A CN2012105685947 A CN 2012105685947A CN 201210568594 A CN201210568594 A CN 201210568594A CN 102974193 A CN102974193 A CN 102974193A
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- Prior art keywords
- tail gas
- tower
- main body
- gas absorber
- float ball
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- Treating Waste Gases (AREA)
Abstract
The invention relates to a tail gas absorbing tower. The tail gas absorbing tower comprises a tower body which is composed of a tower main body and a chimney connected to the top of the tower main body, wherein the tower main body is internally provided with a despumation net, a water mist shower pipe, a pump circulation shower pipe, two internal floating ball grids and a tail gas distributing pipe as well as inner floating balls arranged between the two internal floating ball grids. Compared with the prior art, the tail gas absorbing tower provided by the invention is used for absorbing tail gas containing H2S, SO2, NH3 or phthalic anhydride substances, and has the advantages that the contact area is large, the blockage is prevented, the application range is wide, the energy is saved, the maintenance is convenient, and the like.
Description
Technical field
The present invention relates to a kind of emission-control equipment, especially relate to a kind of tail gas absorber.
Background technology
Processing problem for generation waste gas in chemical industry, the petrochemical industry is the problem of research always, and most of factories use the means of burning or washing tail gas to realize, for H
2S, SO
2, NH
3, the similar substances such as phthalic anhydride, the construction tail gas absorbers that adopt wash more, at present take packed tower as main.
Related documents also discloses the packed tower that is used for absorption tail gas, contact rear absorption tail gas with water by the filler plate in the tower, but the situation that this type of packed tower often stops up, very very complicated is processed in maintenance, and there is cost high, the shortcomings such as aqueous vapor contact area utilization rate is little, and the shower water consumption is large have caused cost to increase and the wasting of resources.
Summary of the invention
Purpose of the present invention be exactly provide in order to overcome the defective that above-mentioned prior art exists a kind of contact area large, prevent from stopping up, tail gas absorber applied widely.
Purpose of the present invention can be achieved through the following technical solutions:
A kind of tail gas absorber comprises:
Tower body: comprise the tower main body and be connected to the chimney at tower main body top;
Tower internals: be located in the tower main body, comprise the foam removal net that sets gradually, water mist sprinkling pipe, pump circulated sprinkling pipe, two inner float ball grids and tail gas distributor pipe from top to bottom;
Inner float ball: be located between two inner float ball grids;
Described tail gas absorber is used for comprising H to containing
2S, SO
2, NH
3Or the absorption of phthalic anhydride material tail gas.
The foam that produces in the described foam removal net interception spray-absorption process prevents that foam is together emptying with tail gas.
The shower water entrance that arranges on the described water mist sprinkling Guan Yuta main body connects.
The circulating pump mouth spray that arranges on the described pump circulated sprinkling Guan Yuta main body connects, and this circulating pump mouth spray is connected with the circulated sprinkling pump through pipeline.
Described inner float ball grid adopts metal or nonmetallic materials to make and obtains.
Described tail gas distributor pipe adopts coil pipe perforating structure, is evenly distributed when tail gas is risen.
The gas inlet that arranges on described tail gas distributor pipe and the tower main body is connected.
Described inner float ball is the polytetrafluoroethylene (PTFE) hollow ball.
Tail gas absorber absorption tail gas of the present invention enters at the bottom of by tower, utilize the rising that evenly distributes of tail gas distributor pipe, air-flow swims in the tower body inner float ball, spray water mist is evenly sprayed from cat head, fully contact with the inner float ball surface, utilize the inner float ball surface moisture to need the material absorbing of washing in the uprising gas, flow down immediately, floss hole is discharged at the bottom of the tower, the long-pending increase of relative contact when having utilized inner float ball to roll, taking full advantage of spray water mist, that tail gas is absorbed is more complete, simultaneously because the floating rolling of spheroid and the phenomenon that can not result in blockage.
Compared with prior art, the present invention has the following advantages:
One, contact area is large: compare with the packed tower of fixed head, and large many of the spheroid contact area of floating rolling, the utilization rate of water also just increases immediately.
Two, prevent from stopping up: the ball float coefficient of friction is little among the present invention, and itself can not stick together, and spheroid is floating rolling in tower, also can not cause the obstruction of grid.
Three, applied widely: the present invention is applicable to H
2S, SO
2, NH
3, the absorption of the similar substances such as phthalic anhydride is made corresponding adjustment, applicable more multimedium to absorbing with liquid and ball float.
Four, energy-conservation: because the utilization rate of water is high, spray-water amount relative reduce.
Five, maintenance is convenient: tower internals of the present invention is simple, overhauls more convenient.
Description of drawings
Fig. 1 is external structure schematic diagram of the present invention;
Fig. 2 is internal structure schematic diagram of the present invention.
Among the figure, N1 is gas inlet, and N2 is the shower water entrance, N3 is exhaust outlet, and N4 is the circulating pump mouth spray, and N5 is waste gas outlet, P is the circulated sprinkling pump, 10 is chimney, and 20 are the foam removal net, and 30 is the water mist sprinkling pipe, 40 is the circulating pump shower, 50 is the inner float ball grid, and 60 is inner float ball, and 70 is the tail gas distributor pipe.
The specific embodiment
The present invention is described in detail below in conjunction with the drawings and specific embodiments.
Embodiment
A kind of tail gas absorber is used for comprising H to containing
2S, SO
2, NH
3Or the absorption of phthalic anhydride material tail gas,
Its structure comprises tower body, tower internals and inner float ball 60 shown in Fig. 1-2.Tower body comprises the tower main body and is connected to the chimney 10 at tower main body top, is provided with gas inlet N1 on the tower main body, shower water entrance N2, exhaust outlet N3, circulating pump mouth spray N4, waste gas outlet N5.Tower internals is located in the tower main body, comprises the foam removal net 20 that sets gradually, water mist sprinkling pipe 30, pump circulated sprinkling pipe 40, two inner float ball grids 50 and tail gas distributor pipe 70 from top to bottom; The foam that produces in the foam removal net 20 interception spray-absorption processes, prevent that foam is together emptying with tail gas, the shower water entrance N2 that arranges on water mist sprinkling pipe 30 and the tower main body is connected, the circulating pump mouth spray that arranges on pump circulated sprinkling pipe 40 and the tower main body is connected N4, and this circulating pump mouth spray N4 is connected with circulated sprinkling pump P through pipeline.The inner float ball grid can adopt metal or nonmetallic materials to make and obtain, tail gas distributor pipe 70 adopts coil pipe perforating structure, when being risen, tail gas is evenly distributed, the gas inlet N1 that arranges on tail gas distributor pipe 70 and the tower main body is connected, the exhaust outlet N3 of tower main body below setting is connected with circulated sprinkling pump P through pipeline in addition, tower main body top offers waste gas outlet N5, and is communicated with chimney 10.The inner float ball 60 that adopts is the polytetrafluoroethylene (PTFE) hollow ball, is located between two inner float ball grids 50.
During use, tail gas entrance N1 at the bottom of the tower enters tower body, evenly rises by tail gas distributor pipe 70, makes the floating rolling of inner float ball; Shower water enters from cat head shower water entrance N2, evenly sprays to inner float ball 60 surfaces by shower 30; Inner float ball 60 is in grid 50 interior activities, and surface moisture fully contacts with rising tail gas; Waste water after the absorption is discharged from the N3 mouth, and it is recycling that part enters circulating pump shower 40 by circulated sprinkling pump P to circulated sprinkling mouth N4, and remainder is disposed to collecting zone; Waste gas after the absorption by the bubble of bringing in the foam removal net 20 interception gases after, from exhaust outlet N5 by chimney 10 emptying.
The tail gas absorber absorption tail gas enters at the bottom of by tower, utilizing tail gas distributor pipe 70 evenly to distribute rises, air-flow swims in the tower body inner float ball 60, spray water mist is evenly sprayed from cat head, fully contact with the surface of inner float ball 60, utilize inner float ball 60 surface moistures to need the material absorbing of washing in the uprising gas, flow down immediately, floss hole is discharged at the bottom of the tower, the long-pending increase of relative contact when having utilized inner float ball 60 to roll, taking full advantage of spray water mist, that tail gas is absorbed is more complete, simultaneously because the floating rolling of spheroid and the phenomenon that can not result in blockage.
Claims (8)
1. a tail gas absorber is characterized in that, this tail gas absorber comprises:
Tower body: comprise the tower main body and be connected to the chimney at tower main body top;
Tower internals: be located in the tower main body, comprise the foam removal net that sets gradually, water mist sprinkling pipe, pump circulated sprinkling pipe, two inner float ball grids and tail gas distributor pipe from top to bottom;
Inner float ball: be located between two inner float ball grids;
Described tail gas absorber is used for comprising H to containing
2S, SO
2, NH
3Or the absorption of phthalic anhydride material tail gas.
2. a kind of tail gas absorber according to claim 1 is characterized in that, the foam that produces in the described foam removal net interception spray-absorption process prevents that foam is together emptying with tail gas.
3. a kind of tail gas absorber according to claim 1 is characterized in that, the shower water entrance that arranges on the described water mist sprinkling Guan Yuta main body connects.
4. a kind of tail gas absorber according to claim 1 is characterized in that, the circulating pump mouth spray that arranges on the described pump circulated sprinkling Guan Yuta main body connects, and this circulating pump mouth spray is connected with the circulated sprinkling pump through pipeline.
5. a kind of tail gas absorber according to claim 1 is characterized in that, described inner float ball grid adopts metal or nonmetallic materials to make and obtains.
6. a kind of tail gas absorber according to claim 1 is characterized in that, described tail gas distributor pipe adopts coil pipe perforating structure, is evenly distributed when tail gas is risen.
7. a kind of tail gas absorber according to claim 1 is characterized in that, the gas inlet that arranges on described tail gas distributor pipe and the tower main body is connected.
8. a kind of tail gas absorber according to claim 1 is characterized in that, described inner float ball is the polytetrafluoroethylene (PTFE) hollow ball.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105685947A CN102974193A (en) | 2012-12-24 | 2012-12-24 | Tail gas absorbing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105685947A CN102974193A (en) | 2012-12-24 | 2012-12-24 | Tail gas absorbing tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102974193A true CN102974193A (en) | 2013-03-20 |
Family
ID=47848711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012105685947A Pending CN102974193A (en) | 2012-12-24 | 2012-12-24 | Tail gas absorbing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102974193A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288142A (en) * | 2013-06-04 | 2013-09-11 | 滨州坤宝化工有限责任公司 | Production process and production equipment for ferric trichloride |
| CN106377990A (en) * | 2016-11-28 | 2017-02-08 | 孟祥寨 | Application of self-made tail gas purification apparatus in chemical production |
| CN106984116A (en) * | 2016-01-20 | 2017-07-28 | 北京中科净原环保科技有限公司 | A kind of gas high-efficient purification tower and gas handling system |
| CN113209785A (en) * | 2021-04-02 | 2021-08-06 | 宁波泽瑞环保科技有限公司 | High-efficient sulphur is retrieved and tail gas processing apparatus |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56163727A (en) * | 1980-05-21 | 1981-12-16 | Kyowa Kako Kk | Gas absorption tower |
| JPS61178020A (en) * | 1985-02-05 | 1986-08-09 | Toshikatsu Suzuki | Apparatus for absorbing exhaust gas |
| CN2105333U (en) * | 1991-10-31 | 1992-05-27 | 成都环保建设工程技术公司 | Floating ball packed tower |
| CN201380038Y (en) * | 2009-01-23 | 2010-01-13 | 江苏新世纪江南环保有限公司 | Grid-type wet desulphurization device |
| CN201969468U (en) * | 2010-12-27 | 2011-09-14 | 北京工业大学 | Gas washing and recovery device for polycarboxylic acid water reducing agent macromonomer preparation |
| CN203061032U (en) * | 2012-12-24 | 2013-07-17 | 上海建安化工设计有限公司 | Tail gas absorbing device |
-
2012
- 2012-12-24 CN CN2012105685947A patent/CN102974193A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56163727A (en) * | 1980-05-21 | 1981-12-16 | Kyowa Kako Kk | Gas absorption tower |
| JPS61178020A (en) * | 1985-02-05 | 1986-08-09 | Toshikatsu Suzuki | Apparatus for absorbing exhaust gas |
| CN2105333U (en) * | 1991-10-31 | 1992-05-27 | 成都环保建设工程技术公司 | Floating ball packed tower |
| CN201380038Y (en) * | 2009-01-23 | 2010-01-13 | 江苏新世纪江南环保有限公司 | Grid-type wet desulphurization device |
| CN201969468U (en) * | 2010-12-27 | 2011-09-14 | 北京工业大学 | Gas washing and recovery device for polycarboxylic acid water reducing agent macromonomer preparation |
| CN203061032U (en) * | 2012-12-24 | 2013-07-17 | 上海建安化工设计有限公司 | Tail gas absorbing device |
Non-Patent Citations (2)
| Title |
|---|
| 卢春喜，王祝安: "《催化裂化流态化技术》", 30 November 2002, 中国石化出版社 * |
| 王晓红等: "《化工原理下册》", 31 July 2012, 化学工业出版社 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288142A (en) * | 2013-06-04 | 2013-09-11 | 滨州坤宝化工有限责任公司 | Production process and production equipment for ferric trichloride |
| CN106984116A (en) * | 2016-01-20 | 2017-07-28 | 北京中科净原环保科技有限公司 | A kind of gas high-efficient purification tower and gas handling system |
| CN106984116B (en) * | 2016-01-20 | 2020-11-13 | 北京中科净原环保科技有限公司 | High-efficient gas purification tower and gas treatment system |
| CN106377990A (en) * | 2016-11-28 | 2017-02-08 | 孟祥寨 | Application of self-made tail gas purification apparatus in chemical production |
| CN113209785A (en) * | 2021-04-02 | 2021-08-06 | 宁波泽瑞环保科技有限公司 | High-efficient sulphur is retrieved and tail gas processing apparatus |
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Application publication date: 20130320 |