CN105056709A - Tail gas processing method - Google Patents
Tail gas processing method Download PDFInfo
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- CN105056709A CN105056709A CN201510457699.9A CN201510457699A CN105056709A CN 105056709 A CN105056709 A CN 105056709A CN 201510457699 A CN201510457699 A CN 201510457699A CN 105056709 A CN105056709 A CN 105056709A
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- absorption tower
- tail gas
- inlet pipe
- pipe
- absorbing liquid
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- Gas Separation By Absorption (AREA)
Abstract
The invention discloses a tail gas processing method. A three-grade counter-current mode is adopted to process the tail gas; a first absorbing tower, a second absorbing tower, and a third absorbing tower are parallelly arranged; the tail gas is connected to a tail gas inlet pipe, and at the same time a water inlet pipe is connected to a water source. The tail gas goes through the first absorbing tower, the second absorbing tower, and the third absorbing tower and finally is discharged out of the system from the gas outlet pipe. The provided method can effectively remove tail gas generated in the electroplate technology and is safe and environment-friendly.
Description
Technical field
The present invention relates to a kind of exhaust gas treating method, specifically a kind of for the exhaust gas treating method in electroplating technology.
Background technology
Along with the reinforcement of environmental consciousness, the requirement of people to environmental protection is more and more higher, the pollution sources of heavy contamination is continued to increase to the dynamics of regulation.At present in electroplating technology, tail gas takes the mode of directly discharge, causes environmental pollution, does not meet environmental requirement.
Summary of the invention
The object of this invention is to provide a kind of exhaust gas treating method, adopt the method can effectively remove the tail gas produced in electroplating technology, safety and environmental protection.Adopt three stage countercurrent modes to absorb waste gas, the amount of conserving water, the tail gas concentration that in first order absorption tower, absorbing liquid absorbs is high, easily process further; Third level absorption tower, absorbing liquid concentration is high, effectively removes waste gas in tail gas.
Object of the present invention is achieved through the following technical solutions:
A kind of exhaust gas treating method, is characterized in that: the method adopts the mode of three stage countercurrents to process tail gas, and concrete steps are as follows:
1) the first absorption tower, second absorption tower and the 3rd absorption tower are arranged in juxtaposition, absorbing liquid is equipped with in single absorption tower, tail gas air inlet pipe A is provided with in the first bottom, absorption tower, exceed absorbing liquid liquid level position be connected with tracheae on the first top, absorption tower, tracheae is connected to second absorption tower bottom, be connected to the 3rd bottom, absorption tower by second absorption tower top, be connected with escape pipe B on the 3rd top, absorption tower; Water inlet pipe C is provided with in the 3rd bottom, absorption tower, water pipe is connected with lower than absorbing liquid liquid level position on the 3rd top, absorption tower, water pipe is connected to second absorption tower bottom, is connected to the first bottom, absorption tower by second absorption tower top, connects outlet pipe D on the first top, absorption tower;
2) be connected to by tail gas on tail gas air inlet pipe A, water inlet pipe C is connected with water source simultaneously;
3) tail gas is after the first absorption tower, second absorption tower and the process of the 3rd absorption tower, is discharged by escape pipe B.
In the present invention, absorbing liquid and tail gas suitable.Absorbing liquid can change targetedly.Safety air vavle is provided with above the first absorption tower, second absorption tower and the 3rd absorption tower.Blowoff valve is provided with bottom the first absorption tower, second absorption tower and the 3rd absorption tower.
It is not very big that the present invention is applicable to tail gas amount, or the system of tail gas composition more complicated, and absorbing liquid can change targetedly.
The present invention can effectively remove the tail gas produced in electroplating technology, safety and environmental protection.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of three stage countercurrent modes in the present invention.
Detailed description of the invention
A kind of exhaust gas treating method, the method adopts the mode of three stage countercurrents to process tail gas, and concrete steps are as follows:
First absorption tower 1, second absorption tower 2 and the 3rd absorption tower 3 are arranged in juxtaposition, absorbing liquid 4 is equipped with in single absorption tower, tail gas air inlet pipe A is provided with in the first bottom, absorption tower, exceed absorbing liquid liquid level position be connected with tracheae 5 on the first top, absorption tower, tracheae is connected to second absorption tower bottom, be connected to the 3rd bottom, absorption tower by second absorption tower top, be connected with escape pipe B on the 3rd top, absorption tower; Water inlet pipe C is provided with in the 3rd bottom, absorption tower, water pipe 6 is connected with lower than absorbing liquid liquid level position on the 3rd top, absorption tower, water pipe is connected to second absorption tower bottom, is connected to the first bottom, absorption tower by second absorption tower top, connects outlet pipe D on the first top, absorption tower;
Be connected to by tail gas on tail gas air inlet pipe A, water inlet pipe C is connected with water source simultaneously;
Tail gas, after the first absorption tower, second absorption tower and the process of the 3rd absorption tower, is discharged by escape pipe B.
Absorbing liquid and tail gas suitable, absorbing liquid can change targetedly.Safety air vavle is provided with above the first absorption tower, second absorption tower and the 3rd absorption tower.Blowoff valve is provided with bottom the first absorption tower, second absorption tower and the 3rd absorption tower.
The present invention can effectively remove the tail gas produced in electroplating technology, safety and environmental protection.
Claims (4)
1. an exhaust gas treating method, is characterized in that: the method adopts the mode of three stage countercurrents to process tail gas, and concrete steps are as follows:
1) the first absorption tower (1), second absorption tower (2) and the 3rd absorption tower (3) are arranged in juxtaposition, absorbing liquid (4) is equipped with in each absorption tower, tail gas air inlet pipe (A) is provided with in the first absorption tower (1) bottom, exceed absorbing liquid (4) liquid level position be connected with tracheae (5) on (1) top, the first absorption tower, tracheae (5) is connected to second absorption tower (2) bottom, be connected to the 3rd absorption tower (3) bottom by second absorption tower (2) top, be connected with escape pipe (B) on the 3rd absorption tower (3) top; Water inlet pipe (C) is provided with in the 3rd absorption tower (3) bottom, water pipe (6) is connected with on the 3rd (3) top, absorption tower lower than absorbing liquid (4) liquid level position, water pipe (6) is connected to second absorption tower (2) bottom, be connected to the first absorption tower (1) bottom by second absorption tower (2) top, connect outlet pipe (D) on the first absorption tower (1) top;
2) be connected to by tail gas in tail gas air inlet pipe (A), water inlet pipe (C) is connected with water source simultaneously;
3) tail gas is after the first absorption tower (1), second absorption tower (2) and the process of the 3rd absorption tower (3), is discharged by escape pipe (B).
2. exhaust gas treating method according to claim 1, is characterized in that: absorbing liquid (4) is suitable with tail gas.
3. exhaust gas treating method according to claim 1, is characterized in that: be provided with safety air vavle in the first absorption tower (1), second absorption tower (2) and top, the 3rd absorption tower (3).
4. exhaust gas treating method according to claim 1, is characterized in that: be provided with blowoff valve in the first absorption tower (1), second absorption tower (2) and bottom, the 3rd absorption tower (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201510457699.9A CN105056709A (en) | 2015-07-30 | 2015-07-30 | Tail gas processing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201510457699.9A CN105056709A (en) | 2015-07-30 | 2015-07-30 | Tail gas processing method |
Publications (1)
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CN105056709A true CN105056709A (en) | 2015-11-18 |
Family
ID=54486349
Family Applications (1)
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CN201510457699.9A Pending CN105056709A (en) | 2015-07-30 | 2015-07-30 | Tail gas processing method |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109603432A (en) * | 2018-11-29 | 2019-04-12 | 成都虹波钼业有限责任公司 | A kind of ammonia-containing exhaust absorbs the processing method of application |
CN112691533A (en) * | 2021-03-23 | 2021-04-23 | 山东金宜善新材料有限公司 | Sodium sulfite absorption tower device |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS5484877A (en) * | 1977-12-19 | 1979-07-06 | Mitsubishi Chem Ind Ltd | Alkali scouring method of gas containing acid gas |
CN1099669A (en) * | 1993-08-30 | 1995-03-08 | 叶树滋 | Method of concentrating low-concentration sulfur dioxide by water absorption method |
CN1118146A (en) * | 1993-02-18 | 1996-03-06 | Abb弗莱克蒂公司 | Process and apparatus for absorbing hydrogen sulphide |
US20040092774A1 (en) * | 2000-10-25 | 2004-05-13 | The Kansai Electric Power Co., Inc. | Amine recovery method and apparatus and decarbonatio apparatus having same |
EP2540376A1 (en) * | 2011-06-29 | 2013-01-02 | IFP Energies nouvelles | Method for deacidifying a gas with a plurality of steps of placing in co-current contact with an absorbent solution |
-
2015
- 2015-07-30 CN CN201510457699.9A patent/CN105056709A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5484877A (en) * | 1977-12-19 | 1979-07-06 | Mitsubishi Chem Ind Ltd | Alkali scouring method of gas containing acid gas |
CN1118146A (en) * | 1993-02-18 | 1996-03-06 | Abb弗莱克蒂公司 | Process and apparatus for absorbing hydrogen sulphide |
CN1099669A (en) * | 1993-08-30 | 1995-03-08 | 叶树滋 | Method of concentrating low-concentration sulfur dioxide by water absorption method |
US20040092774A1 (en) * | 2000-10-25 | 2004-05-13 | The Kansai Electric Power Co., Inc. | Amine recovery method and apparatus and decarbonatio apparatus having same |
EP2540376A1 (en) * | 2011-06-29 | 2013-01-02 | IFP Energies nouvelles | Method for deacidifying a gas with a plurality of steps of placing in co-current contact with an absorbent solution |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109603432A (en) * | 2018-11-29 | 2019-04-12 | 成都虹波钼业有限责任公司 | A kind of ammonia-containing exhaust absorbs the processing method of application |
CN112691533A (en) * | 2021-03-23 | 2021-04-23 | 山东金宜善新材料有限公司 | Sodium sulfite absorption tower device |
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Application publication date: 20151118 |