CN107754556A - A kind of paint industry VOCs processing units - Google Patents

A kind of paint industry VOCs processing units Download PDF

Info

Publication number
CN107754556A
CN107754556A CN201711230302.8A CN201711230302A CN107754556A CN 107754556 A CN107754556 A CN 107754556A CN 201711230302 A CN201711230302 A CN 201711230302A CN 107754556 A CN107754556 A CN 107754556A
Authority
CN
China
Prior art keywords
waste gas
processing units
pipeline
paint industry
vocs processing
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
Application number
CN201711230302.8A
Other languages
Chinese (zh)
Inventor
苏翔宇
任玲辉
陈喆
段英杰
唐开远
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.)
Xi'an Yu Chang Environmental Technology Co Ltd
Original Assignee
Xi'an Yu Chang Environmental Technology Co Ltd
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 Xi'an Yu Chang Environmental Technology Co Ltd filed Critical Xi'an Yu Chang Environmental Technology Co Ltd
Priority to CN201711230302.8A priority Critical patent/CN107754556A/en
Publication of CN107754556A publication Critical patent/CN107754556A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/02Separation 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 by adsorption, e.g. preparative gas chromatography
    • B01D53/06Separation 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 by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0002Casings; Housings; Frame constructions
    • B01D46/0005Mounting of filtering elements within casings, housings or frames
    • B01D46/0008Two or more filter elements not fluidly connected positioned in the same housing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00Specific waste
    • F23G2209/14Gaseous waste or fumes

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention discloses a kind of paint industry VOCs processing units, include waste gas and enter pipeline, waste gas is connected with gas filtration system, zeolite adsorption concentration runner system, rotary RTO systems and chimney into pipeline is suitable successively.A kind of paint industry VOCs processing units of the present invention can utilize the humidity of residual heat of reaction regulation VOCs waste gas.

Description

A kind of paint industry VOCs processing units
Technical field
The invention belongs to organic waste gas treatment device technical field, is related to a kind of paint industry VOCs processing units.
Background technology
Along with the fast development of China's industry, while economy grows at top speed, atmosphere pollution situation also getting worse. Wherein, the discharge of volatile organic matter (VOCs, Volatile Organic Compounds) is cause atmosphere pollution important One of reason, the VOCs waste gas of industrial discharge play critical effect in atmosphere pollution forming process, be cause PM2.5 and O3The important as precursors thing of pollution.VOCs has stronger photo-oxidative, accelerates photochemical reaction, is that secondary organic aerosol is formed Major reason, further produce secondary pollution.At present, the VOCs discharge standards that country and each province and city are put into effect are concentrated mainly on Industrial coating industry, petroleum chemical industry, packages printing industry, industrial coating are also the key industry for turning into the discharge of VOCs waste gas One of.Therefore, country has put into effect a series of laws and regulations, relevant policies file and renovation scheme, it is desirable to increases to industry Application VOCs managements, push forward industrial coating VOCs emission controls comprehensively.The industrial coating VOCs discharges formulated in each province and city In standard, most area requires that highest allows concentration of emission to be 30mg/m3, the VOCs of paint industry administers extremely urgent.
Industrial coating refers to metal and nonmetallic surface protective mulch or decorative layer, and application is a system engineering, It is including the processing before application to coated article surface, spraying coating process and dries three basic working procedures, can all be produced in these processes Raw VOCs discharge.Industrial coating process is mainly used in painting dressing automobiles, Furniture manufacture, engineering machinery and steel construction etc. production During, the VOCs exhaust gas constituents species of discharge is various, selects the equipment of end purified treatment to seem particularly critical.Paint industry VOCs waste gas have the characteristics that air quantity is big, concentration is low, humidity is high, the particle of coating cloud is small in waste gas, viscosity is big, easily sticks.
The content of the invention
It is an object of the invention to provide a kind of paint industry VOCs processing units, can utilize residual heat of reaction regulation VOCs waste gas Humidity.
The technical solution adopted in the present invention is a kind of paint industry VOCs processing units, includes waste gas and enters pipeline, Waste gas is connected with gas filtration system, zeolite adsorption concentration runner system, rotary RTO systems and chimney into pipeline is suitable successively.
It is of the invention to be further characterized in that,
Gas filtration system is three-level filter device.
Three-level filter device includes DPA paint-fog filters, the F7 efficiency filters being sequentially connected according to waste gas approach axis With F9 efficiency filters, F9 efficiency filters connect zeolite adsorption concentration runner system by pipeline.
Be additionally provided with one-level differential pressure pickup between DPA paint-fog filters and F7 efficiency filters, F7 efficiency filters and Two level differential pressure pickup is additionally provided between F9 efficiency filters, between F9 efficiency filters and zeolite adsorption concentration runner system It is additionally provided with three-level differential pressure pickup.
Waste gas is connected with lacquer spraying waste gas pipeline and drying exhaust piping into pipeline, and waste gas, which enters on pipeline, is additionally provided with temperature Humidity sensor.
Zeolite adsorption concentration runner system includes the cooling feed channel being connected respectively with gas filtration system and absorption blower fan, Also include zeolite runner, adsorption zone, desorption area and cooling zone, absorption blower fan connection adsorption zone, absorption are provided with zeolite runner Area is also associated with clean feed channel, and clean feed channel connects chimney, and cooling feed channel is connected with desorption heat exchanger through cooling zone, Desorption heat exchanger is also connected with rotary RTO systems and chimney, and desorption area connects rotary RTO systems also by concentration feed channel, Zeolite runner is also associated with wheel drive means, concentrates and is provided with desorption blower fan in feed channel.
Rotary RTO systems include the main air blower being connected with concentration feed channel, and main air blower is connected with rotary RTO, rotates Formula RTO connection afterheat heat exchangers, afterheat heat exchanger connection chimney.
Combustion chamber that rotary RTO includes setting gradually from top to bottom, regenerator, distributor chamber, go out to enter the room and purge room, go out Side of entering the room is connected with main air blower, and the side relative with main air blower that go out to enter the room is connected with discharge tube, discharge tube connection waste heat Heat exchanger, discharge tube also connect waste gas by wet down admission line and enter pipeline, and combustion chamber is connected by high-temperature pipe and is desorbed Heat exchanger.
Proportioning valve is provided with wet down admission line.
Waste heat pipeline is also associated with afterheat heat exchanger.
The beneficial effects of the invention are as follows:
(1) lacquer spraying waste gas is by with after drying waste gas mixing, helping to reduce the humidity of waste gas, making full use of two kinds of waste gas The characteristics of, and introduce simultaneously rotary RTO waste heat to desorption heat exchanger by the control of the moisture stable of waste gas within 80%, Below 40 DEG C of temperature, save the investment cost of dehumidification equipment, make zeolite adsorption concentration runner system keep higher absorption and It is desorbed efficiency.
(2) lacquer spraying waste gas and drying waste gas participate in Adsorption Concentration together so that the exhausted air quantity for entering rotary RTO processing is big Width reduces, and greatlys save rotary RTO equipment investments and operating cost.
(3) three-level filter device being made up of DPA paint-fog filters, F7 efficiency filters and F9 efficiency filters can ensure that More than 1 μm of coating cloud and impurity will not enter zeolite runner.
(4) air inlet of zeolite runner cooling zone reduces the exhausted air quantity into adsorption zone, helped using the waste gas after filtering In the design capacity for reducing zeolite runner, expense of reducing investment outlay.
(5) zeolite adsorption concentration runner system is applied to processing Wind Volume, the organic exhaust gas of low concentration, and purification efficiency is steady It is fixed, stabilised efficiency is desorbed, operating cost is low, and concentration is up to 20 times.
(6) there was only 25Pa to concentration exhaust piping pressure oscillation during rotary RTO work, contribute to zeolite adsorption concentration to turn The absorption of wheel system and desorption stabilised efficiency, compared to two bed type and three bed RTO there is treatment effeciency to be up to 99.5%, heat profit It is more than 95% with efficiency, key component life length, the features such as floor space is small.
Brief description of the drawings
Fig. 1 is a kind of structural representation of paint industry VOCs processing units of the present invention.
In figure, 1. gas filtration systems, 2. zeolite adsorption concentration runner systems, 3. rotary RTO systems, 4. chimneys;
10. waste gas enters pipeline, 11. Temperature Humidity Sensors, 12. three-level filter devices, 13. wet down admission lines, 14. ratios Example valve;
121.DPA paint-fog filters, 122.F7 efficiency filters, 123.F9 efficiency filters, 124. one-level pressure difference sensings Device, 125. two level differential pressure pickups, 126. three-level differential pressure pickups;
21. adsorbing blower fan, 22. desorption blower fans, 23. zeolite runners, 24. cooling feed channels, 25. clean feed channels, 26. is dense Contracting feed channel, 27. desorption heat exchangers, 28. high temperature feed channels;
231. adsorption zones, 232. desorption areas, 233. cooling zones, 234. wheel drive means;
30. main air blower, 31. rotary RTO, 311. combustion chambers, 312. regenerator, 313. distributor chambers, 314. go out to enter the room, 315. purging rooms, 32. discharge tubes, 33. afterheat heat exchangers, 34. waste heat pipelines.
Embodiment
The present invention is described in detail with reference to the accompanying drawings and detailed description.
A kind of paint industry VOCs processing units, include waste gas and enter pipeline 10, waste gas enters pipeline 10 successively along even There are gas filtration system 1, zeolite adsorption concentration runner system 2, rotary RTO systems 3 and chimney 4.
Gas filtration system 1 is three-level filter device 12.
Three-level filter device 12 includes DPA paint-fog filters 121, the F7 efficiency mistakes being sequentially connected according to waste gas approach axis Filter 122 and F9 efficiency filters 123, F9 efficiency filters 123 connect zeolite adsorption concentration runner system 2 by pipeline.
One-level differential pressure pickup 124, F7 efficiency are additionally provided between DPA paint-fog filters 121 and F7 efficiency filters 122 Two level differential pressure pickup 125, F9 efficiency filters 123 and zeolite are additionally provided between filter 122 and F9 efficiency filters 123 Three-level differential pressure pickup 126 is additionally provided between Adsorption Concentration runner system 2.
Waste gas is connected with lacquer spraying waste gas pipeline and drying exhaust piping into pipeline 10, and waste gas, which enters on pipeline 10, to be also set up There is Temperature Humidity Sensor 11.
Zeolite adsorption concentration runner system 2 includes the cooling feed channel 24 being connected respectively with gas filtration system 1 and absorption Blower fan 21, in addition to zeolite runner 23, adsorption zone 231, desorption area 232 and cooling zone 233, absorption are provided with zeolite runner 23 Blower fan 21 connects adsorption zone 231, and adsorption zone 231 is also associated with clean feed channel 25, and clean feed channel 25 connects chimney 4, cooling Feed channel 24 is connected with desorption heat exchanger 27 through cooling zone 233, and desorption heat exchanger 27 is also connected with rotary RTO systems 3 and cigarette Chimney 4, desorption area 232 connect rotary RTO systems 3 also by concentration feed channel 26, and zeolite runner 23 is also associated with runner driving Device 234, concentrate and desorption blower fan 22 is provided with feed channel 26.
Rotary RTO systems 3 include the main air blower 30 being connected with concentration feed channel 26, and main air blower 30 is connected with rotatably RTO31, rotary RTO31 connections afterheat heat exchanger 33, afterheat heat exchanger 33 connect chimney 4.
Combustion chamber 311 that rotary RTO31 includes setting gradually from top to bottom, regenerator 312, distributor chamber 313, go out to enter the room 314 with purging room 315, and 314 sides that go out to enter the room are connected with main air blower 30, and 314 sides relative with main air blower 30 that go out to enter the room are connected There is discharge tube 32, discharge tube 32 connects afterheat heat exchanger 33, and discharge tube 32 also connects useless by wet down admission line 13 Gas enters pipeline 10, and combustion chamber 311 connects desorption heat exchanger 27 by high-temperature pipe 28.
Proportioning valve 14 is provided with wet down admission line 13.
Waste heat pipeline 34 is also associated with afterheat heat exchanger 33.
A kind of operation principle of paint industry VOCs processing units of the present invention is:
(1) workflow of gas filtration system
The regulation of proportioning valve 14 installed according to the desired value of default by adjusting on wet down admission line 13 enters three The humiture of the level waste gas of filter 12, dries waste gas and lacquer spraying waste gas and the waste gas from rotary RTO discharges passes through jointly Waste gas enters the three-level filter device 12 of pipeline 10, and waste gas sequentially passes through DPA paint-fog filters 121, F7 efficiency filters 122, F9 Efficiency filters 123 are filtered, meanwhile, the work shape of the Real-time Feedback DPA paint-fog filters 121 of one-level differential pressure pickup 124 State, the working condition of the Real-time Feedback F7 efficiency filters 122 of two level differential pressure pickup 125, three-level differential pressure pickup 126 are anti-in real time The working condition of F9 efficiency filters 123 is presented, when filter reaches full load condition, system automatic alarm prompting removable parts Filter, in the small coating cloud particle that waste gas can be effectively gone in removing exhaust gas by three-level filter device 12, contribute to zeolite adsorption The stable operation of concentration runner system 2, extend the service life of zeolite runner 23.
(2) workflow of zeolite adsorption concentration runner system
Zeolite runner 23 is continuously run by wheel drive means 234 with 3-8r/h driven at low speed, through F9 efficiency filters Effect of the waste gas by adsorbing blower fan 21 is blown into adsorption zone 231 after 123 filterings, and the VOCs in waste gas is adsorbed by adsorption zone 231, Clean gas after having adsorbed introduces chimney 35 by clean feed channel 25 and discharged;, will be by cooling zone when going to desorption area 232 233 waste gas is heated to make adsorbed VOCs be desorbed again after introducing desorption area 232 after 180-200 DEG C by desorption heat exchanger 27 Raw, the concentration waste gas after regeneration is sent into rotary RTO systems 3 by the concentrated feed channel 26 of desorption blower fan 22;After the completion of desorption, turn To cooling zone 233, the waste gas after a small amount of filtering is introduced into cooling zone 233 by cooling feed channel 24 and cooled, the boiling after cooling Stone runner 23 continues to adsorb, so circulation;The heat for being desorbed heat exchanger 27 is the high temperature as caused by rotary RTO31 combustion chamber Waste heat is sent into through high-temperature pipe 28.
(3) workflow of rotary RTO systems
After concentration waste gas after desorption and regeneration is sent into rotary RTO systems 3 by main air blower 30, concentration waste gas passes sequentially through out Enter the room 314, distributor chamber 313, regenerator 312, combustion chamber 311, carry out fully burning rear oxidation and decompose, the high temperature after oxidation Decomposition Clean gas passes sequentially through combustion chamber 311, regenerator 312, distributor chamber 313, goes out to enter the room 314, carries out the clean gas one of heat after accumulation of heat Part by discharge tube 32 after afterheat heat exchanger 33 cools after introduce chimney 35 discharge, another part passes through wet down admission line 13, which enter waste gas, enters in pipeline 10 for adjusting waste gas humidity;Heat can by waste heat pipeline 34 caused by afterheat heat exchanger 33 For returning to production line or workshop;Purging room 315 is that the VOCs remained in heat storage is sent into the high temperature again of combustion chamber 311 Oxidation Decomposition.Rotary RTO systems 3 can effectively purified treatment VOCs, while the heat too many levels for again discharging VOCs is efficient Utilize.
The DPA paint-fog filters of the present invention are made of a kind of synthetic materials, and the windward side of filter uses 3D honeycomb stratiforms Structure design meets in-depth filtration principle, can be with 99.8% seizure to more than 10 microns of small coating clouds.DPA paint-fog filters select Brand is Suzhou Mount Tai wound, the differential pressure pickup installed after DPA paint-fog filters, can monitor DPA paint-fog filters in real time Working condition, in the case where reaching full load condition system automatic alarm prompt removable parts filter.
Waste gas after present invention filtering carries out checking concentration by zeolite adsorption concentration runner system, and concentration waste gas is meeting A large amount of waste heats are produced again while the rotary RTO self-operatings in end.The heat for being desorbed heat exchanger produces 800 using rotary RTO DEG C high temperature air, realizes the efficient utilization of waste heat.
Rotary RTO systems enter accumulation of heat body region by waste gas is concentrated by rotary distributor alternating uniformly continuous, in fact Accumulation of heat, the switching of heat release operating mode of continuous and stable are showed, rotary RTO goes out the hot-air of discharge of entering the room through afterheat heat exchanger by heat For returning to production line or workshop, the efficient utilization of waste heat is realized, saves energy consumption.

Claims (10)

1. a kind of paint industry VOCs processing units, it is characterised in that include waste gas and enter pipeline (10), the waste gas enters Pipeline (10) successively along be connected with gas filtration system (1), zeolite adsorption concentration runner system (2), rotary RTO systems (3) and Chimney (4).
A kind of 2. paint industry VOCs processing units according to claim 1, it is characterised in that the gas filtration system (1) it is three-level filter device (12).
A kind of 3. paint industry VOCs processing units according to claim 2, it is characterised in that the three-level filter device (12) DPA paint-fog filters (121), F7 efficiency filters (122) and the F9 effect being sequentially connected according to waste gas approach axis are included Rate filter (123), the F9 efficiency filters (123) connect zeolite adsorption concentration runner system (2) by pipeline.
A kind of 4. paint industry VOCs processing units according to claim 3, it is characterised in that the DPA coating clouds filtering One-level differential pressure pickup (124), the F7 efficiency filters are additionally provided between device (121) and F7 efficiency filters (122) (122) two level differential pressure pickup (125), the F9 efficiency filters (123) are additionally provided between F9 efficiency filters (123) Three-level differential pressure pickup (126) is additionally provided between zeolite adsorption concentration runner system (2).
5. a kind of paint industry VOCs processing units according to claim 1, it is characterised in that the waste gas enters pipeline (10) lacquer spraying waste gas pipeline and drying exhaust piping are connected with, the waste gas, which enters on pipeline (10), is additionally provided with temperature and humidity sensing Device (11).
A kind of 6. paint industry VOCs processing units according to claim 1, it is characterised in that the zeolite adsorption concentration Runner system (2) includes the cooling feed channel (24) being connected respectively with gas filtration system (1) and absorption blower fan (21), in addition to Zeolite runner (23), adsorption zone (231), desorption area (232) and cooling zone (233), institute are provided with the zeolite runner (23) Absorption blower fan (21) connection adsorption zone (231) is stated, the adsorption zone (231) is also associated with clean feed channel (25), the cleaning Feed channel (25) connection chimney (4), the cooling feed channel (24) are connected with desorption heat exchanger (27) through cooling zone (233), The desorption heat exchanger (27) is also connected with the rotary RTO systems (3) and chimney (4), and desorption area (232) is also by dense Contracting feed channel (26) connects rotary RTO systems (3), and the zeolite runner (23) is also associated with wheel drive means (234), institute State and desorption blower fan (22) is provided with concentration feed channel (26).
A kind of 7. paint industry VOCs processing units according to claim 6, it is characterised in that rotary RTO systems (3) Including the main air blower (30) being connected with concentration feed channel (26), the main air blower (30) is connected with rotary RTO (31), the rotation Rotatable RTO (31) connection afterheat heat exchanger (33), afterheat heat exchanger (33) the connection chimney (4).
A kind of 8. paint industry VOCs processing units according to claim 7, it is characterised in that the rotary RTO (31) combustion chamber (311) that includes setting gradually from top to bottom, regenerator (312), distributor chamber (313), go out to enter the room (314) and blow Room (315) is swept, (314) side that goes out to enter the room is connected with the main air blower (30), go out to enter the room (314) and the main air blower (30) Relative side is connected with discharge tube (32), and the discharge tube (32) connects the afterheat heat exchanger (33), the discharge Pipeline (32) also connects the waste gas by wet down admission line (13) and enters pipeline (10), and the combustion chamber (311) passes through height Warm pipeline (28) the connection desorption heat exchanger (27).
A kind of 9. paint industry VOCs processing units according to claim 8, it is characterised in that the wet down admission line (13) proportioning valve (14) is provided with.
10. according to a kind of any described paint industry VOCs processing units of claim 7-9, it is characterised in that the waste heat Waste heat pipeline (34) is also associated with heat exchanger (33).
CN201711230302.8A 2017-11-29 2017-11-29 A kind of paint industry VOCs processing units Pending CN107754556A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711230302.8A CN107754556A (en) 2017-11-29 2017-11-29 A kind of paint industry VOCs processing units

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711230302.8A CN107754556A (en) 2017-11-29 2017-11-29 A kind of paint industry VOCs processing units

Publications (1)

Publication Number Publication Date
CN107754556A true CN107754556A (en) 2018-03-06

Family

ID=61276401

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711230302.8A Pending CN107754556A (en) 2017-11-29 2017-11-29 A kind of paint industry VOCs processing units

Country Status (1)

Country Link
CN (1) CN107754556A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109442441A (en) * 2018-12-03 2019-03-08 汕头东风印刷股份有限公司 A kind of processing system of organic exhaust gas
CN110394042A (en) * 2018-04-25 2019-11-01 杭州中兵环保股份有限公司 Reclaimed rubber waste gas purification apparatus and method
CN110567263A (en) * 2019-09-17 2019-12-13 上海兰宝环保科技有限公司 volatile organic compound source control and terminal treatment system
CN111085082A (en) * 2019-12-31 2020-05-01 江苏大东新材料科技有限公司 Waste gas treatment device
CN111408197A (en) * 2020-03-04 2020-07-14 上海兰宝环保科技有限公司 Device for purifying banburying waste gas in rubber industry and using method
CN111450649A (en) * 2020-05-18 2020-07-28 安徽华菱汽车有限公司 Coating waste gas treatment system and treatment method
CN113384993A (en) * 2021-04-30 2021-09-14 宇星科技发展(深圳)有限公司 VOCs treatment system and method
CN113440981A (en) * 2021-07-08 2021-09-28 厦门宇春环保科技有限公司 Organic waste gas treatment system, treatment process and production workshop
CN113521891A (en) * 2021-06-21 2021-10-22 郑州日产汽车有限公司 Modular VOCs processing system
CN113797707A (en) * 2021-09-25 2021-12-17 益清源环保科技(苏州)有限公司 Hydrophobic zeolite runner is established ties and is had a heat accumulation formula and burn burning furnace

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103007682A (en) * 2012-12-03 2013-04-03 北汽(广州)汽车有限公司 Waste gas treatment method and system of coating workshop based on concentrated runner and RTO (regenerative thermal oxidizer)
CN204485594U (en) * 2015-03-18 2015-07-22 北京鞍信天硕工程技术有限公司 Based on color-coating line exhaust-gas treatment and the heat recovery system of concentration runner and RTO
CN205252836U (en) * 2015-11-13 2016-05-25 惠州市环发环保科技有限公司 Runner adsorbs concentrated RTO waste gas treatment system
CN105854514A (en) * 2016-06-27 2016-08-17 江苏骠马智能装备股份有限公司 Waste gas concentration recycling process on basis of zeolite rollers
CN206343049U (en) * 2016-12-29 2017-07-21 河北九源环保工程有限公司 Integral type organic waste gas purifying processing device
CN207805325U (en) * 2017-11-29 2018-09-04 西安昱昌环境科技有限公司 VOCs processing units for paint industry

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103007682A (en) * 2012-12-03 2013-04-03 北汽(广州)汽车有限公司 Waste gas treatment method and system of coating workshop based on concentrated runner and RTO (regenerative thermal oxidizer)
CN204485594U (en) * 2015-03-18 2015-07-22 北京鞍信天硕工程技术有限公司 Based on color-coating line exhaust-gas treatment and the heat recovery system of concentration runner and RTO
CN205252836U (en) * 2015-11-13 2016-05-25 惠州市环发环保科技有限公司 Runner adsorbs concentrated RTO waste gas treatment system
CN105854514A (en) * 2016-06-27 2016-08-17 江苏骠马智能装备股份有限公司 Waste gas concentration recycling process on basis of zeolite rollers
CN206343049U (en) * 2016-12-29 2017-07-21 河北九源环保工程有限公司 Integral type organic waste gas purifying processing device
CN207805325U (en) * 2017-11-29 2018-09-04 西安昱昌环境科技有限公司 VOCs processing units for paint industry

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110394042A (en) * 2018-04-25 2019-11-01 杭州中兵环保股份有限公司 Reclaimed rubber waste gas purification apparatus and method
CN109442441A (en) * 2018-12-03 2019-03-08 汕头东风印刷股份有限公司 A kind of processing system of organic exhaust gas
CN110567263A (en) * 2019-09-17 2019-12-13 上海兰宝环保科技有限公司 volatile organic compound source control and terminal treatment system
CN111085082A (en) * 2019-12-31 2020-05-01 江苏大东新材料科技有限公司 Waste gas treatment device
CN111085082B (en) * 2019-12-31 2021-10-15 江苏大东新材料科技有限公司 Waste gas treatment device
CN111408197A (en) * 2020-03-04 2020-07-14 上海兰宝环保科技有限公司 Device for purifying banburying waste gas in rubber industry and using method
CN111450649A (en) * 2020-05-18 2020-07-28 安徽华菱汽车有限公司 Coating waste gas treatment system and treatment method
CN113384993A (en) * 2021-04-30 2021-09-14 宇星科技发展(深圳)有限公司 VOCs treatment system and method
CN113521891A (en) * 2021-06-21 2021-10-22 郑州日产汽车有限公司 Modular VOCs processing system
CN113440981A (en) * 2021-07-08 2021-09-28 厦门宇春环保科技有限公司 Organic waste gas treatment system, treatment process and production workshop
CN113797707A (en) * 2021-09-25 2021-12-17 益清源环保科技(苏州)有限公司 Hydrophobic zeolite runner is established ties and is had a heat accumulation formula and burn burning furnace

Similar Documents

Publication Publication Date Title
CN107754556A (en) A kind of paint industry VOCs processing units
CN207805325U (en) VOCs processing units for paint industry
WO2021000621A1 (en) Voc waste gas treatment and purification device and baking finish house provided with same
CN205886514U (en) Paint spraying waste gas treatment device
CN105169886B (en) Energy-efficient large-wind-volume low-concentration organic exhaust gas recycling and administration device and method
JP5744488B2 (en) Exhaust gas treatment equipment
CN105749695A (en) Low concentration, large wind volume and high odor waste gas concentration energization equipment and technology thereof
CN206073094U (en) A kind of VOC waste gas total system
CN104923010B (en) A kind of industrial coating ambient exhaust gas recovering and purifying system
CN204952595U (en) Wet coating exhaust recycling treatment system
CN208809745U (en) A kind of molecular sieve adsorption runner system handling exhaust gas
CN205760438U (en) A kind of activated carbon adsorption concentration for processing VOCs and the integrating device of regenerative thermal oxidizer
CN101062458A (en) Asphalt smoke gas purifying technique
CN206715626U (en) Runner high efficiency cleaning system
WO2018036562A1 (en) Switching concentration-type regenerative catalytic combustion system for organic waste gas treatment
CN110898557A (en) Spray drying room
CN112657330A (en) Volatile organic waste gas treatment process and device in tire industry
CN109432944A (en) Spray the purification concentration cycles method and system of exhaust gas
CN207024949U (en) The industrial dense catalytic thermal burning processing system of VOC waste gas
CN109865629B (en) Energy-saving emission-reducing paint spray booth circulating air system
CN106621759A (en) Automobile 4S store spraying waste gas treatment device and technology thereof
CN201493221U (en) Dry type paint spraying equipment with deep processing device of waste gas
CN108499314A (en) A kind of exhaust treatment system and waste gas treatment equipment
CN204448403U (en) A kind of paint line device for purifying and treating tail gas
CN106582275A (en) Automobile spray-coating baking waste gas control and treatment system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
CB03 Change of inventor or designer information

Inventor after: Ren Linghui

Inventor after: Chen Zhe

Inventor after: Duan Yingjie

Inventor after: Wang Zhibin

Inventor after: Gao Jianbin

Inventor after: Wang Hengtao

Inventor after: Tang Kaiyuan

Inventor before: Su Xiangyu

Inventor before: Ren Linghui

Inventor before: Chen Zhe

Inventor before: Duan Yingjie

Inventor before: Tang Kaiyuan

CB03 Change of inventor or designer information