CN104524966A - Spray coating waste gas biological purification composite treatment method - Google Patents

Spray coating waste gas biological purification composite treatment method Download PDF

Info

Publication number
CN104524966A
CN104524966A CN201410722698.8A CN201410722698A CN104524966A CN 104524966 A CN104524966 A CN 104524966A CN 201410722698 A CN201410722698 A CN 201410722698A CN 104524966 A CN104524966 A CN 104524966A
Authority
CN
China
Prior art keywords
waste gas
mud
reactor
nutrient solution
spray coating
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.)
Granted
Application number
CN201410722698.8A
Other languages
Chinese (zh)
Other versions
CN104524966B (en
Inventor
王灿
胡清源
张悦涛
袁媛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TIANJIN WATERKING MEMBRANE TECHNOLOGY Co Ltd
Tianjin University
Original Assignee
TIANJIN WATERKING MEMBRANE TECHNOLOGY Co Ltd
Tianjin University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TIANJIN WATERKING MEMBRANE TECHNOLOGY Co Ltd, Tianjin University filed Critical TIANJIN WATERKING MEMBRANE TECHNOLOGY Co Ltd
Priority to CN201410722698.8A priority Critical patent/CN104524966B/en
Publication of CN104524966A publication Critical patent/CN104524966A/en
Application granted granted Critical
Publication of CN104524966B publication Critical patent/CN104524966B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

The invention discloses a spray coating waste gas biological purification composite treatment method comprising the following steps: (1) spray coating waste gas is delivered into a fiber cotton filtering device mounted with glass fiber filter cotton; (2) waste gas filtered by the glass fiber filtering device is delivered into a reactor with a filling material in a way that the waste gas enters from the bottom and leaves from the top, and is subjected to biological filtering; at a same time, the filling material is subjected to nutrient solution spraying with a flow pattern from top to bottom from the top of the reactor, such that a carbon source and other elements needed by microbe growth are provided. The method has the following advantages: with the method, paint mist and main pollutants such as toluene, xylene and non-methane hydrocarbon volatile matters produced during a spray coating process can be highly efficiently removed.

Description

A kind of spraying exhaust gas biological purifying combination treatment method
Technical field
The present invention relates to technical field of environmental management, particularly one spraying waste gas combined treatment process.
Background technology
The spraying such as automotive lacquer, furniture application industry can produce a large amount of coating coating clouds in production engineering, and containing VOCs (VOCs) such as the toluene of higher concentration, dimethylbenzene and NMHCs in waste gas.
These VOCs not only produce spread effect to human body, serious threat human health, and alkene in organic compound and some arene compound, in an atmosphere, under the effect of sunlight, can also and nitrogen oxide react and form the photochemical fog of Los Angeles type or industrial photochemical fog, cause secondary pollution, ecological environment damaged.Therefore, the process for the spraying coating cloud that produces of industry and VOC seems very urgent.
At present, mainly in the majority with physico-chemical process to the treatment technology of VOC, mainly contain active carbon adsorption, Physical Absorption method, Production by Catalytic Combustion Process and membrane absorption method.In addition, biofiltration process in recent years due to it has that removal efficiency is high, operating cost is low and the advantage such as less formation secondary pollution by extensive concern.
Biofiltration process mainly utilizes high efficiency packing rapid mass transfer, the characteristic of absorption and the specific function of microorganism, makes waste gas enter filling surface rapidly, contacts with microorganism, thus by VOCs mass degradation or change into some harmless or low harmful class materials.But, utilize independent bio-filter technology to carry out process to spraying waste gas and cannot reach good removal effect.Mainly because the spraying existed in spraying waste gas not only can reduce the removal effect of biofiltration device, and abrasion and corrosion can be caused to the body of device.
Summary of the invention
The object of the invention is to the shortcoming overcoming prior art, a kind of spraying exhaust gas biological purifying combination treatment method efficiently removing the major pollutants such as coating cloud and toluene, dimethylbenzene, NMHC produced in painting process is provided.
In order to achieve the above object, the technical solution used in the present invention is:
One spraying exhaust gas biological purifying combination treatment method of the present invention, it comprises the following steps:
(1) spraying waste gas is passed into the cellucotton filter that glass fiber filter cotton is housed;
(2) sent in the mode of bottom in and top out by the waste gas after filtering through glass fiber filtration apparatus and fill Packed reactor and carry out biofiltration, the spray of nutrient solution is carried out to provide other elements beyond the carbon source needed for growth of microorganism with the type of flow from top to bottom to filler in autoreactor top simultaneously;
The preparation method of described filler comprises the following steps:
A () gets sewage disposal plant aeration tank activated sludge;
B () by mud aeration every day 6-10 hour, and adds the medicine be made up of benzene and dimethylbenzene and tames mud, described benzene, the percent by volume of dimethylbenzene are 1:1-1:1.5, and described mud and the volume ratio of medicine are 60:1-80:1; Tame, after 15-20 days, mud and high-efficiency activated carbon mixture are injected biofiltration reactor, make mud in activated carbon surface biofilm, as filler;
Described nutrient solution prescription is in grams per liter, composed of the following components:
The invention has the advantages that: (1) combines the kinds of processes technology such as filtration, biodegradation and charcoal absorption, efficiently can remove the major pollutants such as coating cloud and toluene, dimethylbenzene, NMHC produced in painting process; (2) there is good adaptability, the purified treatment of high concentration, atm number, different gaseous material can be adapted to; (3) process operation is simple to operate, is easy to safeguard, reduces expense.(4) microorganism colonization method easily realizes, and is conducive to growth of microorganism, completes the quick adsorption of gas, mass transport process, and meanwhile, microbial nutrient solution method for making is simple, with low cost, easy to operate, can provide comprehensive nutrition to microorganism.
Accompanying drawing explanation
Accompanying drawing is a kind of process chart spraying exhaust gas biological purifying combination treatment method of the present invention.
Detailed description of the invention
Describe the present invention below in conjunction with specific embodiment.
One spraying exhaust gas biological purifying combination treatment method of the present invention as shown in drawings, it comprises the following steps: spraying waste gas is passed into the cellucotton filter 1 that glass fiber filter cotton is housed by (1); (2) sent in the mode of bottom in and top out by the waste gas after filtering through glass fiber filtration apparatus and fill Packed reactor 2 and carry out biofiltration, the spray of nutrient solution 3 is carried out to provide other elements beyond the carbon source needed for growth of microorganism with the type of flow from top to bottom to filler in autoreactor top simultaneously;
The preparation method of described filler comprises the following steps:
A () gets sewage disposal plant aeration tank activated sludge;
B () by mud aeration every day 6-10 hour, and adds the medicine be made up of benzene and dimethylbenzene and tames mud, described benzene, the percent by volume of dimethylbenzene are 1:1-1:1.5, and described mud and the volume ratio of medicine are 60:1-80:1; Tame, after 15-20 days, mud and high-efficiency activated carbon mixture are injected biofiltration reactor, make mud in activated carbon surface biofilm, as filler;
Described nutrient solution prescription is in grams per liter, composed of the following components:
The preparation method of described nutrient solution is: mixed by nutrient solution prescription.
The device realizing the inventive method can comprise the cellucotton filter 1 that glass fiber filter cotton is housed, have spraying exhaust gas inlet in the bottom of described cellucotton filter 1 and have spraying waste gas outlet on the top of cellucotton filter 1, described spraying waste gas outlet is connected with the import filling Packed reactor by waste gas pipeline, the import of described reactor is arranged in the reactor shell of filler bottom of reactor, the reactor shell on the filler top of described reactor has the outlet of process gas, in described reactor, filler top is provided with spray equipment, described spray equipment is connected with the storage tank that nutrient solution 3 is housed by the spray piping that measuring pump is housed, the end face and bottom surface of described filler are respectively arranged with water distributing plate and supporting layer, be respectively used to water distribution uniformity and support filler.
Embodiment 1
(1) spraying waste gas is passed into the cellucotton filter that glass fiber filter cotton is housed; (2) sent in the mode of bottom in and top out by the waste gas after filtering through glass fiber filtration apparatus and fill Packed reactor and carry out biofiltration, the spray of nutrient solution 3 is carried out to provide other elements beyond the carbon source needed for growth of microorganism with the type of flow from top to bottom to filler in autoreactor top simultaneously;
The preparation method of described filler comprises the following steps:
A () gets sewage disposal plant aeration tank activated sludge;
B () by mud aeration every day 6 hours, and adds the medicine be made up of benzene and dimethylbenzene and tames mud, described benzene, the percent by volume of dimethylbenzene are 1:1, and described mud and the volume ratio of medicine are 80:1; Tame, after 17 days, mud and high-efficiency activated carbon mixture are injected biofiltration reactor, make mud in activated carbon surface biofilm, as filler;
Described nutrient solution prescription is in grams per liter, composed of the following components:
The preparation method of described nutrient solution is: mixed by nutrient solution prescription.
Adopt this method, process certain paint spray booth waste gas.Average exhaust amount is 14000m 3/ h, in exhaust, TVOC concentration is 500-650mg/m 3, after adopting cellucotton filtration-biofiltration combined treatment process to process, exit TVOC concentration is 50-75mg/m 3, clearance reaches more than 85%.
Embodiment 2
(1) spraying waste gas is passed into the cellucotton filter that glass fiber filter cotton is housed; (2) sent in the mode of bottom in and top out by the waste gas after filtering through glass fiber filtration apparatus and fill Packed reactor and carry out biofiltration, the spray of nutrient solution 3 is carried out to provide other elements beyond the carbon source needed for growth of microorganism with the type of flow from top to bottom to filler in autoreactor top simultaneously;
The preparation method of described filler comprises the following steps:
A () gets sewage disposal plant aeration tank activated sludge;
B () by mud aeration every day 8 hours, and adds the medicine be made up of benzene and dimethylbenzene and tames mud, described benzene, the percent by volume of dimethylbenzene are 1:1.5, and described mud and the volume ratio of medicine are 60:1; Tame, after 15 days, mud and high-efficiency activated carbon mixture are injected biofiltration reactor, make mud in activated carbon surface biofilm, as filler;
Described nutrient solution prescription is in grams per liter, composed of the following components:
The preparation method of described nutrient solution is: mixed by nutrient solution prescription.
Adopt this method: process air quantity is 16000m 3certain painting workshop waste gas of/h, TVOC concentration is 350-450mg/m 3, after the process of cellucotton filtration-biofiltration combined treatment process, TVOC concentration is about 32mg/m 3, clearance reaches 91%-93%.
Embodiment 3
(1) spraying waste gas is passed into the cellucotton filter that glass fiber filter cotton is housed; (2) sent in the mode of bottom in and top out by the waste gas after filtering through glass fiber filtration apparatus and fill Packed reactor and carry out biofiltration, the spray of nutrient solution 3 is carried out to provide other elements beyond the carbon source needed for growth of microorganism with the type of flow from top to bottom to filler in autoreactor top simultaneously;
The preparation method of described filler comprises the following steps:
A () gets sewage disposal plant aeration tank activated sludge;
B () by mud aeration every day 10 hours, and adds the medicine be made up of benzene and dimethylbenzene and tames mud, described benzene, the percent by volume of dimethylbenzene are 1:1.05, and described mud and the volume ratio of medicine are 72:1; Tame, after 20 days, mud and high-efficiency activated carbon mixture are injected biofiltration reactor, make mud in activated carbon surface biofilm, as filler;
Described nutrient solution prescription is in grams per liter, composed of the following components:
The preparation method of described nutrient solution is: mixed by nutrient solution prescription.
Adopt this method: the waste gas processing certain timber processing paint shop.It is 40000m that this workshop produces waste gas air quantity 3/ h, TVOC concentration is 500-650mg/m 3, after the process of cellucotton filtration-biofiltration combined treatment process, exit TVOC concentration is 35-80mg/m 3, TVOC clearance reaches 85%-95%.

Claims (1)

1. spray an exhaust gas biological purifying combination treatment method, it is characterized in that, it comprises the following steps:
(1) spraying waste gas is passed into the cellucotton filter that glass fiber filter cotton is housed;
(2) sent in the mode of bottom in and top out by the waste gas after filtering through glass fiber filtration apparatus and fill Packed reactor and carry out biofiltration, the spray of nutrient solution is carried out to provide other elements beyond the carbon source needed for growth of microorganism with the type of flow from top to bottom to filler in autoreactor top simultaneously;
The preparation method of described filler comprises the following steps:
A () gets sewage disposal plant aeration tank activated sludge;
B () by mud aeration every day 6-10 hour, and adds the medicine be made up of benzene and dimethylbenzene and tames mud, described benzene, the percent by volume of dimethylbenzene are 1:1-1:1.5, and described mud and the volume ratio of medicine are 60:1-80:1; Tame, after 15-20 days, mud and high-efficiency activated carbon mixture are injected biofiltration reactor, make mud in activated carbon surface biofilm, as filler;
Described nutrient solution prescription is in grams per liter, composed of the following components:
CN201410722698.8A 2014-12-02 2014-12-02 A kind of spraying exhaust gas biological purifying combination treatment method Active CN104524966B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410722698.8A CN104524966B (en) 2014-12-02 2014-12-02 A kind of spraying exhaust gas biological purifying combination treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410722698.8A CN104524966B (en) 2014-12-02 2014-12-02 A kind of spraying exhaust gas biological purifying combination treatment method

Publications (2)

Publication Number Publication Date
CN104524966A true CN104524966A (en) 2015-04-22
CN104524966B CN104524966B (en) 2016-08-24

Family

ID=52840699

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410722698.8A Active CN104524966B (en) 2014-12-02 2014-12-02 A kind of spraying exhaust gas biological purifying combination treatment method

Country Status (1)

Country Link
CN (1) CN104524966B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104826483A (en) * 2015-05-25 2015-08-12 永康市禄祥环保科技有限公司 Paint spraying waste gas and organic waste gas biological purification method

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040219657A1 (en) * 2003-04-29 2004-11-04 National Chiao Tung University System and process for treating waste gas employing bio-treatment technology
CN1745883A (en) * 2004-09-11 2006-03-15 中国石油化工股份有限公司 Purification for stink and organic waste gas
CN101058055A (en) * 2007-06-01 2007-10-24 哈尔滨工业大学 Biologically deodorizing method
CN101259367A (en) * 2008-04-17 2008-09-10 东北电力大学 Technique and device for simultaneously removing malodor of multiple gas mixture
CN101264421A (en) * 2008-03-20 2008-09-17 湖南大学 Biological filtering device for treating toluene gas
JP2009106805A (en) * 2007-10-26 2009-05-21 Hitachi Plant Technologies Ltd Voc gas treatment method
CN202569894U (en) * 2012-06-12 2012-12-05 中国国际海运集装箱(集团)股份有限公司 Painting organic waste gas recovery processing device

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040219657A1 (en) * 2003-04-29 2004-11-04 National Chiao Tung University System and process for treating waste gas employing bio-treatment technology
CN1745883A (en) * 2004-09-11 2006-03-15 中国石油化工股份有限公司 Purification for stink and organic waste gas
CN101058055A (en) * 2007-06-01 2007-10-24 哈尔滨工业大学 Biologically deodorizing method
JP2009106805A (en) * 2007-10-26 2009-05-21 Hitachi Plant Technologies Ltd Voc gas treatment method
CN101264421A (en) * 2008-03-20 2008-09-17 湖南大学 Biological filtering device for treating toluene gas
CN101259367A (en) * 2008-04-17 2008-09-10 东北电力大学 Technique and device for simultaneously removing malodor of multiple gas mixture
CN202569894U (en) * 2012-06-12 2012-12-05 中国国际海运集装箱(集团)股份有限公司 Painting organic waste gas recovery processing device

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
孔鑫等: "温度对生物过滤塔填料层含水率和运行性能的影响", 《环境科学学报》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104826483A (en) * 2015-05-25 2015-08-12 永康市禄祥环保科技有限公司 Paint spraying waste gas and organic waste gas biological purification method

Also Published As

Publication number Publication date
CN104524966B (en) 2016-08-24

Similar Documents

Publication Publication Date Title
CN203725007U (en) Exhaust gas microwave catalytic purification device
Wang et al. Enhanced removal of ethylbenzene from gas streams in biotrickling filters by Tween-20 and Zn (II)
CN103239986B (en) Biological filtering device and technology for treating organic waste gas
CN202289835U (en) Organic waste gas purifying system
CN101259367A (en) Technique and device for simultaneously removing malodor of multiple gas mixture
CN105233640A (en) System for purifying volatile organic compounds exhaust gas through plasma synergistic biological technology
CN205340577U (en) Two -way rotary spraying industrial waste gas purifier
CN104984638A (en) Multiple effect integrated waste gas purification system
CN105311931A (en) Industrial VOC waste gas decomposition purification treatment method and equipment
CN105498523A (en) Waste gas treatment system
CN205199268U (en) Industry VOCs waste gas decomposes purifier treatment equipment
CN202860343U (en) Novel smelly waste gas treatment device
CN204429095U (en) A kind of spraying exhaust gas biological purifying combined treatment device
CN104524966B (en) A kind of spraying exhaust gas biological purifying combination treatment method
CN204219998U (en) A kind of off-gas cleaning equipment
CN105664710A (en) Method for treating paint-spraying volatile organic waste gas in coating workshop
CN205042336U (en) System for plasma biotechnology in coordination purifies volatile organic compounds waste gas
CN205084565U (en) Environment -friendly workshop exhaust gas purification device
CN208553742U (en) One kind being used for the multi-level biological cleaning processing unit of organic exhaust gas
CN1242836C (en) Process for cleaning waste gas
CN105289156A (en) Paint-spraying exhaust-gas processing technology
CN205269343U (en) Exhaust purification treatment facility
CN1362280A (en) Waste gas purifier
CN203990300U (en) For the device of purifying and stive-aromatic hydrocarbons organic exhaust gas
CN208553694U (en) One kind being used for organic exhaust gas multi-stage biological purifying processing device

Legal Events

Date Code Title Description
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant