CN105536465A - Waste gas treatment system - Google Patents
Waste gas treatment system Download PDFInfo
- Publication number
- CN105536465A CN105536465A CN201610048936.0A CN201610048936A CN105536465A CN 105536465 A CN105536465 A CN 105536465A CN 201610048936 A CN201610048936 A CN 201610048936A CN 105536465 A CN105536465 A CN 105536465A
- Authority
- CN
- China
- Prior art keywords
- waste gas
- treatment system
- catalytic oxidation
- oxidation tower
- spray column
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8678—Removing components of undefined structure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/2073—Manganese
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The invention discloses a waste gas treatment system which comprises a spray tower, an activated carbon adsorption box connected with the output end of the top of the spray tower and a catalytic oxidation tower connected with the output end of the activated carbon adsorption box. The waste gas treatment system comprises the following steps that (A) waste gas is pumped into a spray tower through a fan, a PH regulator is added into the spray tower to keep a PH valve in the spray tower to be 6-9; (B) the waste gas subjected to the step (A) flows into an activated carbon adsorption box from the top of the spray tower to adsorb peculiar smell in the waste gas; (C) the waste gas subjected to the step (B) flows into a catalytic oxidation tower to remove OH free radicals through reaction and enables clean air to be discharged out of the catalytic oxidation tower and discharge clean water from the bottom of the catalytic oxidation tower, and waste gas treatment is completed. When the waste gas treatment system is used, the dosage is greatly decreased, accordingly secondary pollution is reduced, the energy consumption and cost are effectively reduced, meanwhile absolutely clean air and clean water are discharged out of the system, and the waste gas treatment system is good in applicability and practicability.
Description
Technical field
The invention belongs to technical field of waste gas treatment, be specifically related to a kind of exhaust treatment system.
Background technology
Exhaust-gas treatment has multiple method, as spray process, blow-off method, active carbon adsorption, plasma method etc., but have that chemical feeding quantity is large, secondary pollution, occupation of land space is large, cost is high problem, and need different processing be built to different pollution factor, Meteorological is large, so that practitioner is kept within bounds and interferes with the development.
Summary of the invention
In order to solve the problems of the technologies described above, the present invention be to provide a kind of stability in use good, take up an area the little and exhaust treatment system that cost is low in space.
The technical scheme realizing the object of the invention is a kind of exhaust treatment system, and the catalytic oxidation tower comprising spray column, the active carbon adsorption case be connected with described spray column top output port and be connected with described active carbon adsorption case output, comprises following treatment step
Steps A, waste gas to be pumped in spray column through blower fan, and in spray column, increase PH conditioning agent, make pH value in spray column remain on 6-9;
Step B, enter in active carbon adsorption case from the top of spray column, by the peculiar smell adsorption in waste gas through the waste gas of steps A;
Step C, enter in catalytic oxidation tower through the waste gas of step B, OH radical reaction is removed, the top of pure air autocatalyzed oxidation tower is discharged and clean water is discharged from the bottom of catalytic oxidation tower, complete exhaust-gas treatment.
Manganese sand catalytic reaction layer is provided with in described catalytic oxidation tower.
In step C, waste gas with hydroxyl oxygen agent for 0.2ml/M
3spray is on manganese sand catalytic reaction layer.
PH conditioning agent is acid medicine in step.
The present invention has positive effect: the present invention greatly reduces chemical feeding quantity in use, thus decreases secondary pollution, and effectively reduces energy consumption and cost, and simultaneously it discharges the air of absolute cleanliness and clean water, and applicability is good, practical.
Accompanying drawing explanation
In order to make content of the present invention be more likely to be clearly understood, below according to specific embodiment also by reference to the accompanying drawings, the present invention is further detailed explanation, wherein:
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
(embodiment 1)
Fig. 1 shows a kind of detailed description of the invention of the present invention, and wherein Fig. 1 is structural representation of the present invention.
See Fig. 1, a kind of exhaust treatment system, the catalytic oxidation tower 3 comprising spray column 1, the active carbon adsorption case 2 be connected with described spray column 1 top output port and be connected with described active carbon adsorption case 2 output, comprises following treatment step
Steps A, waste gas to be pumped in spray column through blower fan, and in spray column, increase PH conditioning agent, make pH value in spray column remain on 6-9;
Step B, enter in active carbon adsorption case from the top of spray column, by the peculiar smell adsorption in waste gas through the waste gas of steps A;
Step C, enter in catalytic oxidation tower through the waste gas of step B, OH radical reaction is removed, the top of pure air autocatalyzed oxidation tower is discharged and clean water is discharged from the bottom of catalytic oxidation tower, complete exhaust-gas treatment.
Manganese sand catalytic reaction layer is provided with in described catalytic oxidation tower.
In step C, waste gas with hydroxyl oxygen agent for 0.2ml/M
3spray is on manganese sand catalytic reaction layer.
PH conditioning agent is acid medicine in step.
The present invention greatly reduces chemical feeding quantity in use, thus decreases secondary pollution, and effectively reduces energy consumption and cost, and simultaneously it discharges the air of absolute cleanliness and clean water, and applicability is good, practical.
Obviously, the above embodiment of the present invention is only for example of the present invention is clearly described, and is not the restriction to embodiments of the present invention.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And these belong to connotation of the present invention the apparent change of extending out or variation still belong to protection scope of the present invention.
Claims (4)
1. an exhaust treatment system, the catalytic oxidation tower comprising spray column, the active carbon adsorption case be connected with described spray column top output port and be connected with described active carbon adsorption case output, is characterized in that: comprise following treatment step
Steps A, waste gas to be pumped in spray column through blower fan, and in spray column, increase PH conditioning agent, make pH value in spray column remain on 6-9;
Step B, enter in active carbon adsorption case from the top of spray column, by the peculiar smell adsorption in waste gas through the waste gas of steps A;
Step C, enter in catalytic oxidation tower through the waste gas of step B, OH radical reaction is removed, the top of pure air autocatalyzed oxidation tower is discharged and clean water is discharged from the bottom of catalytic oxidation tower, complete exhaust-gas treatment.
2. exhaust treatment system according to claim 1, is characterized in that: in described catalytic oxidation tower, be provided with manganese sand catalytic reaction layer.
3. exhaust treatment system according to claim 2, is characterized in that: in step C, waste gas with hydroxyl oxygen agent for 0.2ml/M
3spray is on manganese sand catalytic reaction layer.
4. exhaust treatment system according to claim 3, is characterized in that: PH conditioning agent is acid medicine in step.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610048936.0A CN105536465A (en) | 2016-01-26 | 2016-01-26 | Waste gas treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610048936.0A CN105536465A (en) | 2016-01-26 | 2016-01-26 | Waste gas treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105536465A true CN105536465A (en) | 2016-05-04 |
Family
ID=55816311
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610048936.0A Pending CN105536465A (en) | 2016-01-26 | 2016-01-26 | Waste gas treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105536465A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108128927A (en) * | 2017-12-28 | 2018-06-08 | 吉林建筑大学 | A kind of method for removing lead ion in water removal using sulphite reinforcing manganese sand |
| CN108619887A (en) * | 2018-05-17 | 2018-10-09 | 绍兴市鼎泰节能环保科技有限公司 | A kind of exhaust treatment system |
| CN110057979A (en) * | 2019-04-27 | 2019-07-26 | 东莞市创拓信息科技有限公司 | Atmosphere control emission monitoring system and method |
| CN112892166A (en) * | 2021-01-22 | 2021-06-04 | 西安交通大学 | System and method for eliminating harmful gas in closed space |
| CN114288834A (en) * | 2021-12-27 | 2022-04-08 | 深圳职业技术学院 | Advanced oxidation system and method for treating organic waste gas based on carbon activated persulfate |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070086931A1 (en) * | 2005-06-13 | 2007-04-19 | Applied Materials, Inc. | Methods and apparatus for process abatement |
| CN101496993A (en) * | 2009-01-07 | 2009-08-05 | 上海水天环保科技有限公司 | Method and device for processing malodorous gas by active bamboo charcoal-H2O2 complex phase catalytic oxidation |
| CN202289838U (en) * | 2011-10-10 | 2012-07-04 | 山东天兴生物科技有限公司 | Tail gas treatment device for sebacic acid |
| US20140348741A1 (en) * | 2013-05-23 | 2014-11-27 | Linde Aktiengesellschaft | Process and apparatus for treating a sulphur-containing off-gas from a sulphur recovery system |
| CN204294099U (en) * | 2014-12-09 | 2015-04-29 | 淄博宝泉环保工程有限公司 | A kind of industrial waste gas controlling device |
-
2016
- 2016-01-26 CN CN201610048936.0A patent/CN105536465A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070086931A1 (en) * | 2005-06-13 | 2007-04-19 | Applied Materials, Inc. | Methods and apparatus for process abatement |
| CN101496993A (en) * | 2009-01-07 | 2009-08-05 | 上海水天环保科技有限公司 | Method and device for processing malodorous gas by active bamboo charcoal-H2O2 complex phase catalytic oxidation |
| CN202289838U (en) * | 2011-10-10 | 2012-07-04 | 山东天兴生物科技有限公司 | Tail gas treatment device for sebacic acid |
| US20140348741A1 (en) * | 2013-05-23 | 2014-11-27 | Linde Aktiengesellschaft | Process and apparatus for treating a sulphur-containing off-gas from a sulphur recovery system |
| CN204294099U (en) * | 2014-12-09 | 2015-04-29 | 淄博宝泉环保工程有限公司 | A kind of industrial waste gas controlling device |
Non-Patent Citations (1)
| Title |
|---|
| 童志权，陈焕钦: "《工业废气污染控制与利用》", 31 January 1989, 化学工业出版社 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108128927A (en) * | 2017-12-28 | 2018-06-08 | 吉林建筑大学 | A kind of method for removing lead ion in water removal using sulphite reinforcing manganese sand |
| CN108619887A (en) * | 2018-05-17 | 2018-10-09 | 绍兴市鼎泰节能环保科技有限公司 | A kind of exhaust treatment system |
| CN110057979A (en) * | 2019-04-27 | 2019-07-26 | 东莞市创拓信息科技有限公司 | Atmosphere control emission monitoring system and method |
| CN112892166A (en) * | 2021-01-22 | 2021-06-04 | 西安交通大学 | System and method for eliminating harmful gas in closed space |
| CN114288834A (en) * | 2021-12-27 | 2022-04-08 | 深圳职业技术学院 | Advanced oxidation system and method for treating organic waste gas based on carbon activated persulfate |
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Application publication date: 20160504 |