CN208612188U - Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment - Google Patents

Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment Download PDF

Info

Publication number
CN208612188U
CN208612188U CN201821076171.2U CN201821076171U CN208612188U CN 208612188 U CN208612188 U CN 208612188U CN 201821076171 U CN201821076171 U CN 201821076171U CN 208612188 U CN208612188 U CN 208612188U
Authority
CN
China
Prior art keywords
desorption
air
exhaust gas
blower
organic exhaust
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.)
Expired - Fee Related
Application number
CN201821076171.2U
Other languages
Chinese (zh)
Inventor
王国栋
杨学谦
李有森
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.)
Dalian Juyang Technology Co Ltd
Original Assignee
Dalian Juyang 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 Dalian Juyang Technology Co Ltd filed Critical Dalian Juyang Technology Co Ltd
Priority to CN201821076171.2U priority Critical patent/CN208612188U/en
Application granted granted Critical
Publication of CN208612188U publication Critical patent/CN208612188U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Of Gases By Adsorption (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

The utility model provides organic exhaust gas rotation enriched catalytic oxidation integrated equipment, belong to pollution technical field of air purification, utilize adsorption/desorption integrated catalytic oxidation technology to external coating more particularly to a kind of, the device that the volatile organic contaminant discharged when the industry productions operation such as packages printing is administered, including sequentially connected blast pipe, coating cloud separator, absorber, catalytic oxidizer, distribution mixer, residual-heat exchanger, adsorb blower, blower is desorbed, fresh air-cooler, air-exhausting duct and chimney composition, it is mainly used for the emission pollution problem for solving low concentration Wind Volume industrial organic exhaust gas, with energy-efficient, component is compact, space occupied is small, the advantages of high degree of automation.

Description

Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment
Technical field
The utility model belongs to atmosphere polluting controling technology field, and in particular to a kind of adsorption/desorption integrated catalytic oxidation skill The device that the volatile organic contaminant discharged when art is to the industry productions operation such as external coating, packages printing is administered.
Background technique
It is often generated largely in processes such as the various drying tunnels of industries, the surface lacquers such as mechanical part, building materials furniture, car and boat manufacture Coating cloud particle and solvent volatilize exhaust gas, and ingredient is mainly the aromatic hydrocarbons such as benzene homologues, esters, ketone or oxygen-containing class organic compound, Inorganization distributes or in line into atmosphere with different approach in workshop, not only causes air pollution, is detrimental to health simultaneously. Organic exhaust gas majority is discharged after the absorption of single-activity charcoal using after cascade sedimentation coating cloud particle at present, since cascade settles Coating cloud low efficiency often leads to adsorbing medium hole plug and activated carbon adsorption saturation, needs to frequently replace active carbon, time-consuming to take Power causes artificial and cost huge waste.Traditional adsorption/desorption catalyzing oxidation unit is using water spray except coating cloud device, suction Attached desorption apparatus, catalytic oxidizing equipment single module series design, control valve is more and complicated for operation, and system structure is also huge Greatly, it is limited by plant area, enterprise space, is unable to satisfy mounting condition, and existing equipment is preferably to realize desorption temperature, it is most Directly exchanged heat using fresh air with heat exchanger, not only cost of manufacture is high, it is desirable that fresh blower mesh power it is also larger and remaining The problems such as heat utilization efficiency is low, excessive generation carbon emission.
Summary of the invention
To solve the above-mentioned problems, the purpose of this utility model is that: provide organic exhaust gas rotation enriched catalytic oxidation Integrated equipment is mainly used for solving the pollution problem of low concentration Wind Volume organic exhaust gas, has purification efficiency height, component tight It gathers, the advantages of space occupied is small, equipment investment and operating cost are low, safe and reliable, high degree of automation, is that one kind is worthy to be popularized Environmental protection equipment.
The utility model is achieved through the following technical solutions: organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment, Including sequentially connected blast pipe, coating cloud separator, absorber, catalytic oxidizer, distribution mixer, residual-heat exchanger, absorption Blower, desorption blower, fresh air-cooler, air-exhausting duct and chimney composition;Coating cloud separator is placed in the lower section of absorber, coating cloud separator Entrance connect with blast pipe by air distribution plate, the outlet of coating cloud separator passes through the connection absorber air inlet of electrokinetic adsorption intake valve Mouthful, absorber gas outlet is connect by electrokinetic adsorption air outlet valve with air-exhausting duct, is arranged Xiang great Qi through absorption blower and chimney, is catalyzed oxygen Change device outlet to connect with the purified gas entrance of the high temperature branch pipe of distribution mixer and residual-heat exchanger respectively by triple valve, waste heat The clean gas outlet of exchanger is connect with chimney, and the gas outlet of fresh air-cooler is connect with the low temperature branch pipe of distribution mixer, distribution The mixing branch pipe of mixer is connect by the way that pipeline is desorbed with electronic desorption intake valve, electronic desorption intake valve and electrokinetic adsorption outlet Bypass line below valve connects, and the bypass above electrokinetic adsorption intake valve is equipped with electronic desorption air outlet valve, electronic desorption outlet Valve is connected by the desorption gas entrance of pipeline and residual-heat exchanger, and the desorption gas outlet of residual-heat exchanger is through desorption blower and catalysis The connection of oxidator air inlet.
The coating cloud separator, is made of stainless steel cloth, all-glass paper, air distribution plate and pressing plate, the glass Fibrous paper is set between stainless steel cloth, and the stainless steel wire thickness of net is not less than 3 centimetres, at least 2 layers of stainless steel cloth quantity.
Concentration monitor sensor is provided with below the electrokinetic adsorption air outlet valve and electronic desorption air outlet valve.
The utility model has the following beneficial effects: 1. by being all provided with below electrokinetic adsorption air outlet valve and electronic desorption air outlet valve Concentration monitor sensor is set, to the on-line monitoring for judging adsorption saturation, clean level being desorbed, and realization and PLC control are chain, Accurate switching rotation adsorption/desorption working procedure, makes operation be optimal effect;2. being substituted in integrated equipment with distribution mixer Heat-exchange system not only reduces the air quantity that fresh blower introduces, it may also reduce the discharge amount of high temperature carbonaceous gas.
Detailed description of the invention
Fig. 1 is the structure chart of the utility model;
Fig. 2 is coating cloud cyclone separator arrangement schematic diagram.
Specific embodiment
Below in conjunction with attached drawing, the utility model is described in further detail.Attached drawing is simplified schematic diagram only to show Meaning mode illustrates the basic structure of the utility model, therefore it only shows composition related with the utility model.
Organic exhaust gas rotation enriched catalytic as shown in Figure 1 and Figure 2 aoxidizes integrated equipment, including sequentially connected blast pipe (1), coating cloud separator (2), absorber (3), catalytic oxidizer (4), distribution mixer (5), residual-heat exchanger (6) adsorb blower (7), blower (8), fresh air-cooler (9), air-exhausting duct (10) and chimney (11) composition is desorbed;Coating cloud separator (2) is placed in absorber (3) entrance of lower section, coating cloud separator (2) is connect by air distribution plate (23) with blast pipe (1), and coating cloud separator (2) goes out Mouth connects absorber (3) air inlet by electrokinetic adsorption intake valve (31), and absorber (3) gas outlet passes through electrokinetic adsorption air outlet valve (32) it is connect with air-exhausting duct (9), arranges Xiang great Qi through absorption blower (7) and chimney (10), catalytic oxidizer (4) outlet passes through threeway Valve is connect with the purified gas entrance (61) of the high temperature branch pipe (51) of distribution mixer (5) and residual-heat exchanger (6) respectively, and waste heat is handed over The clean gas outlet (62) of parallel operation (6) is connect with chimney (11), and the gas outlet of fresh air-cooler (9) is low with distribution mixer (5) Warm branch pipe (52) connection, the mixing branch pipe (53) of distribution mixer (5) are connected by desorption pipeline and electronic desorption intake valve (41) It connects, electronic desorption intake valve (41) connect with the bypass line below electrokinetic adsorption air outlet valve (32), electrokinetic adsorption intake valve (31) bypass above is equipped with electronic desorption air outlet valve (42), and electronic desorption air outlet valve (42) passes through pipeline and residual-heat exchanger (6) desorption gas entrance (63) connection, the desorption gas outlet (64) of residual-heat exchanger (6) is through desorption blower (8) and catalysis oxidation The connection of device (4) air inlet.
The coating cloud separator (2), by stainless steel cloth (21), all-glass paper (22), air distribution plate (23) and pressing plate (24) it constitutes, the all-glass paper (22) is set between stainless steel cloth (21), and stainless steel cloth (21) thickness is not Less than 3 centimetres, at least 2 layers of stainless steel cloth (21) quantity.
Concentration monitor sensor is provided with below the electrokinetic adsorption air outlet valve and electronic desorption air outlet valve (42) (12)。
Organic gas is first pumped organic gas to coating cloud point by blast pipe (1) by the suction of absorption blower (7) After being filtered out above coating cloud separator (2) from the organic gas carried out in device (2) except coating cloud particle, after except coating cloud particle, By open electrokinetic adsorption intake valve (31) enter absorber (3), at this point, electronic desorption air outlet valve (42) and it is electronic be desorbed into Air valve (41) is in off state, and the absorber (3) that organic gas is largely filled adsorbing medium material is adsorbed, Shao Liangwei The gas being adsorbed is through electrokinetic adsorption air outlet valve (32), air-exhausting duct (10) and chimney (11) qualified discharge;When some absorber (3) Concentration monitor sensor (12) below corresponding electrokinetic adsorption air outlet valve detects discharge gas concentration beyond the dense of setting When spending lower limit, system opens catalytic oxidizer (4), and starting desorption blower (8) opens simultaneously electronic desorption air outlet valve (42) and electricity Dynamic desorption intake valve (41), and close adsorption saturation the corresponding electrokinetic adsorption intake valve (31) of absorber (3) and electronic suction Attached air outlet valve (32), at this point, forming desorption circuit.It is blown since the strong suction of blower (8) is desorbed, and by fresh air-cooler (9) One clean air enters distribution mixer (5), and circulated air circulation is formed in desorption system, after fresh wind is heated, one Hot gas enters distribution mixer (5) by high temperature branch pipe (51) and is mixed with the fresh cold air come in from low temperature branch pipe (52), Mixed gas from top to bottom carries out the absorber of adsorption saturation (3) through electronic desorption intake valve (41) through mixing branch pipe (53) Purging work, another blast of hot air make to be desorbed after the high concentration organic gas come out is heated up by heat exchange again by residual-heat exchanger (6) It returns to and carries out oxygenolysis in catalytic oxidizer (4), realize the utilization of waste heat, reduce the burning in catalytic oxidizer (4) Warm energy is mended, more energy saving, the High Temperature Gas after decomposing in catalytic oxidizer (4) participates in gas distribution mixing and waste heat again Exchange utilizes, when the concentration monitor sensor (12) below electronic desorption intake valve (42) shows that numerical value reaches design requirement, Terminate desorption process, enters the adsorption/desorption cyclic process of next absorber (3) according to the method described above, meanwhile, it is completed de- The absorber (3) of attached work carries out cooling stand-by.
The preferable specific embodiment of the above, only the utility model, but the protection scope of the utility model is not It is confined to this, anyone skilled in the art is practical according to this in the technical scope that the utility model discloses Novel technical solution and its inventive concept is subject to equivalent substitution or change, should all cover the protection scope of the utility model it It is interior.

Claims (3)

1. organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment, including sequentially connected blast pipe, coating cloud separator, absorption Device, catalytic oxidizer, distribution mixer, residual-heat exchanger, absorption blower, desorption blower, fresh air-cooler, air-exhausting duct and chimney group At;It is characterized in that, the coating cloud separator is placed in the lower section of absorber, the entrance of coating cloud separator passes through air distribution plate and air inlet The outlet of pipe connection, coating cloud separator connects absorber air inlet by electrokinetic adsorption intake valve, and absorber gas outlet passes through electricity Dynamic adsorption outlet valve is connect with air-exhausting duct, arranges Xiang great Qi through absorption blower and chimney, catalytic oxidizer outlet passes through triple valve point Do not connect with the purified gas entrance of the high temperature branch pipe of distribution mixer and residual-heat exchanger, the clean gas outlet of residual-heat exchanger with Chimney connection, the gas outlet of fresh air-cooler are connect with the low temperature branch pipe of distribution mixer, and the mixing branch pipe of distribution mixer passes through Desorption pipeline is connect with electronic desorption intake valve, and the bypass line below electronic desorption intake valve and electrokinetic adsorption air outlet valve connects It connects, the bypass above electrokinetic adsorption intake valve is equipped with electronic desorption air outlet valve, and electronic desorption air outlet valve is handed over by pipeline and waste heat The desorption gas entrance of parallel operation connects, and the desorption gas outlet of residual-heat exchanger is connected through desorption blower with catalytic oxidizer air inlet.
2. organic exhaust gas rotation enriched catalytic according to claim 1 aoxidizes integrated equipment, it is characterised in that: the paint Mist separator is made of stainless steel cloth, all-glass paper, air distribution plate and pressing plate, and the all-glass paper is set to stainless steel Between silk screen, the stainless steel wire thickness of net is not less than 3 centimetres, at least 2 layers of stainless steel cloth quantity.
3. organic exhaust gas rotation enriched catalytic according to claim 1 aoxidizes integrated equipment, it is characterised in that: the electricity Concentration monitor sensor is provided with below dynamic adsorption outlet valve and electronic desorption air outlet valve.
CN201821076171.2U 2018-07-09 2018-07-09 Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment Expired - Fee Related CN208612188U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821076171.2U CN208612188U (en) 2018-07-09 2018-07-09 Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821076171.2U CN208612188U (en) 2018-07-09 2018-07-09 Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment

Publications (1)

Publication Number Publication Date
CN208612188U true CN208612188U (en) 2019-03-19

Family

ID=65705230

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821076171.2U Expired - Fee Related CN208612188U (en) 2018-07-09 2018-07-09 Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment

Country Status (1)

Country Link
CN (1) CN208612188U (en)

Similar Documents

Publication Publication Date Title
CN104492255A (en) Method for treating waste gas through adsorption-ozone-catalysis together with adsorption material in-situ regeneration
CN206073094U (en) A kind of VOC waste gas total system
CN105944500B (en) The cellular VOCs adsorption/desorptions device and method of fixed-bed type
CN107051110A (en) Lacquer spraying waste gas processing equipment and its handling process
CN208541981U (en) Organic waste gas treatment system
CN107694282A (en) Utilize the technique and device of activated carbon processing organic exhaust gas
CN109381964A (en) Organic exhaust gas recovery and processing system and method
CN108079738B (en) Energy-saving environment-friendly circulating type waste gas treatment method applied to paint spraying and baking process
CN101062458A (en) Asphalt smoke gas purifying technique
CN205517124U (en) Organic waste gas processing apparatus based on fixed molecular sieve adsorption bed
CN208612188U (en) Organic exhaust gas rotates enriched catalytic and aoxidizes integrated equipment
CN218469604U (en) Gas capture system for capturing carbon dioxide from cement kiln flue gas
CN107029516A (en) A kind of spray painting tail gas treatment device for collecting Adsorption Concentration and high-speed catalysis burning
CN208130771U (en) A kind of organic waste gas treatment device
CN206823466U (en) Lacquer spraying waste gas processing equipment
CN207614590U (en) High-efficient organic waste gas dry-type preprocessing device
CN106076062A (en) Lacquer spraying waste gas processing system
CN205867917U (en) Spray paint waste gas treatment system
CN215233307U (en) High-efficient processing system of volatile organic compounds
CN207445896U (en) A kind of adsorption and desorption is catalyzed burning waste gas processing equipment
CN209917582U (en) Rotary drum adsorption concentration device
CN209630919U (en) Spray exhaust gas environmental protection purifying equipment
CN106568302A (en) Drying device for the production of honeycomb ceramic body SCR denitration catalyst
CN112675703A (en) Efficient volatile organic compound treatment system and method
CN207137694U (en) A kind of decentralised adsorption concentrates the VOC processing systems of regeneration

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190319