CN206008465U - A kind of organic waste gas treatment system - Google Patents

A kind of organic waste gas treatment system Download PDF

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Publication number
CN206008465U
CN206008465U CN201620744049.2U CN201620744049U CN206008465U CN 206008465 U CN206008465 U CN 206008465U CN 201620744049 U CN201620744049 U CN 201620744049U CN 206008465 U CN206008465 U CN 206008465U
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CN
China
Prior art keywords
gas
waste gas
discharge duct
sack cleaner
treatment system
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
CN201620744049.2U
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Chinese (zh)
Inventor
贾建洪
周士晖
吕杭杰
陶嘉贵
李非里
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Hangzhou Bo Yi Yi Environmental Technology Co Ltd
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Hangzhou Bo Yi Yi Environmental Technology Co Ltd
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Publication date
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Priority to CN201620744049.2U priority Critical patent/CN206008465U/en
Application granted granted Critical
Publication of CN206008465U publication Critical patent/CN206008465U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Treating Waste Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

The utility model discloses a kind of organic waste gas treatment system, including admission line and discharge duct, it is characterized in that, also include sack cleaner and the spray column being sequentially connected by gas pipeline, the admission line is connected with the air inlet of sack cleaner, the discharge duct is connected with the gas outlet of spray column, is provided with least one absorbing unit, is provided with least one drying unit in the discharge duct in the gas pipeline between the low-light resonance exhaust processor and sack cleaner.After waste gas is processed by the utility model via dedusting, photochemical catalytic oxidation and deodorization, so that waste gas is effectively purified, it is particularly suited for processing the organic exhaust gas produced in DYE PRODUCTION, treatment effect is preferable, so that waste gas obtains discharging standards, meet environmental requirement.

Description

A kind of organic waste gas treatment system
Technical field
The utility model belongs to technical field of waste gas treatment, and in particular to a kind of organic waste gas treatment system.
Background technology
With current industry and commerce development and the enhancing of environmental consciousness, the society that be subject to that goes from bad to worse of living environment With the most attention of industrial circle, wherein, due to flourishing for industry, air pollution diffusion is rapid, the face that harmful exhaust is stretched The healthy of vast polluter direct harm people through respiratory system in waste gas is accumulated, for this development trend, various Technology and equipment with regard to environment-friendly engineering is constantly developed therewith.About the purified treatment of industrial waste gas, then it is many environmental protection One of faced most important problem in case.
During existing industrial waste gas is processed, a lot of waste gas processing methods are occurred in that, such as low-light resonance exhaust processor is to adopt Purified with microwave plus photooxidation catalytic waste gas and combined, by microwave energizer and conversion equipment, supporting independent stainless steel group Part, in independent limited space, strongly excites electrodeless lamp tube, obtains the extraordinary ultraviolet of high output.High-strength special type is purple Outside line and microwave mutually strengthen in independent resonator, produce a large amount of ozone and free hydroxyl, strong destruction and oxidation gaseous effluent Molecule, so that reach the purpose of VOCs treatment.
The species of existing process waste gas is a lot, for example, produce the enterprise of dye and dye intermediate, in process of production first With formaldehyde condensation, neutralization, dry production dye dispersant MF (poly- naphthalene formaldehyde sulfonate salt) after base naphthalene sulfonation, during being somebody's turn to do, there is portion Methyl naphthalene and substantial amounts of formaldehyde gas is divided to produce, if will cause to surrounding environment and plant area's enterprise employee health without effective process huge Big impact.At present during such exhaust-gas treatment, dedusting is carried out to waste gas first, is then processed by deodorization, the processing method is to gas Dust removal effect is preferable, but little to the removal effect of organic matter, and gas sweetening effect is poor, and organic exhaust gas effect reaches Less than discharging standards.
Utility model content
The utility model provides a kind of organic waste gas treatment system, can be to the organic exhaust gas of generation during DYE PRODUCTION Effectively processed, made up to discharging standards.
The technical solution of the utility model is:A kind of organic waste gas treatment system, including admission line and discharge duct, also Including the sack cleaner that is sequentially connected by gas pipeline and spray column, the air inlet of the admission line and sack cleaner Mouthful it is connected, the discharge duct is connected with the gas outlet of spray column, the low-light resonance exhaust processor and bag-type dust At least one absorbing unit is provided with gas pipeline between device, is provided with least one drying unit in the discharge duct.
The organic exhaust gas produced during the utility model DYE PRODUCTION are when being processed, first by organic exhaust gas via entering Feed channel enter sack cleaner carry out dedusting, through sack cleaner dedusting after, waste gas enter gas pipeline in, enter back into spray Drenching in tower carries out Water spray process, for sloughing the unstable ozone in part, the taste of gas is removed.After due to Water spray, In waste gas may remnant steam, when the waste gas after the utility model deodorization is discharged via discharge duct, can be via row Drying unit in feed channel is dried, and finally discharges via discharge duct.
Preferably, being provided with low-light resonance exhaust processor between the sack cleaner and spray column.
Preferably, being provided with least one in gas pipeline between the low-light resonance exhaust processor and sack cleaner Individual absorbing unit,
Due to being provided with absorbing unit in the conveyance conduit between sack cleaner and low-light resonance exhaust processor, therefore give up During gas is conveyed in the gas pipeline, carry out preliminary decolorization adsorption and process, finally low-light is entered via gas pipeline Resonance exhaust processor is processed, and low-light resonance exhaust processor is very strong using the effect generation oxidability of photochemical catalytic oxidation Hydroxyl radical free radical and free oxygen radical, the organic principle in oxidizing gas, using microwave high energy high-penetrability, further break Emission molecule chain is split, a high oxidation body (being commonly called as " plasma-based ") is produced, high oxidation body one kind is higher by 2000 than ozone oxidation ability Many times of oxysome, can be by the organic matter exhaustive oxidation in waste gas into H2O and CO2.
In the utility model, waste gas can pass through each absorbing unit one by one, so as to disposably realize the multistage suction to waste gas Attached, it is ensured that absorption completely, is seamlessly connected between multi-stage absorption, is simplified adsorption step, is greatlyd save manpower.In the same manner, drying unit Similarly.
Preferably, the absorbing unit is the absorption cavity for being filled with adsorbent in the utility model, the absorption cavity Two side walls consistent with gas flow are the gas permeation net that supplied gas are passed through.The aperture of gas permeation net is will not make suction Attached dose spills while beneficial to gas by being advisable.
Preferably, the adsorbent is acticarbon.Acticarbon has physical absorption and chemisorbed Double grading, can selectively adsorb the various materials in gas phase, with reach decolorizing and refining, disinfecting, deodorizing and decontamination purification Etc. purpose.
Preferably, the drying unit be filled with drier dry cavity, this dries cavity and gas flow one The two side walls for causing are the gas permeation net that supplied gas are passed through.The aperture of gas permeation net spill will not drier, with When beneficial to gas by being advisable.In the utility model, drier can have multiple, such as silica.
Preferably, the discharge duct is helix tube.The path of helix tube is longer, can slow down waste gas in discharge duct In transfer rate, extend the time of contact of waste gas and drying unit, improve drying effect.
Preferably, the admission line is helix tube.The path of helix tube is longer, can slow down waste gas in admission line In transfer rate, extend waste gas and absorbing unit time of contact, improve adsorption effect.
Compared with prior art, the beneficial effects of the utility model are embodied in:
After waste gas is processed by the utility model via dedusting, photochemical catalytic oxidation and deodorization so that waste gas is obtained effectively Purification, be particularly suited in DYE PRODUCTION produce organic exhaust gas process, treatment effect is preferable so that waste gas is obtained Discharging standards, meet environmental requirement.
Description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
As shown in figure 1, the utility model includes admission line 1 and discharge duct 2, also include by gas pipeline 3 successively The sack cleaner 4 of connection, low-light resonance exhaust processor 5 and spray column 6, wherein admission line 1 and sack cleaner 4 Air inlet is connected, and discharge duct 2 is connected with the gas outlet of spray column 6, low-light resonance exhaust processor 5 and sack cleaner At least one absorbing unit 31 is provided with gas pipeline 3 between 4, is provided with least one drying unit 21 in blast pipe 2.
In the utility model, admission line 1 and discharge duct 2 are helix tube.The path of helix tube is longer, can slow down The transfer rate of waste gas, extends waste gas and drying unit and the time of contact of absorbing unit, improves and dry and adsorption effect.
Also shown in FIG. 1, in the utility model, absorbing unit 31 is the absorption cavity 312 for being filled with adsorbent 311, should Absorption cavity 312 two side walls consistent with gas flow are the gas permeation net 313 that supplied gas are passed through.Gas permeation net 313 aperture is spill will not adsorbent 311 while beneficial to gas by being advisable.In the utility model, adsorbent 311 is work Property carbon adsorbent.Acticarbon has the double grading of physical absorption and chemisorbed, can selectively adsorb gas phase In various materials, with reach decolorizing and refining, disinfecting, deodorizing and decontamination purification etc. purpose.
As shown in figure 1, drying unit 21 dries cavity 22 for be filled with drier 211 in the utility model, the drying The two side walls consistent with gas flow of cavity 212 are the gas permeation net 213 that supplied gas are passed through.Gas permeation net 213 Aperture is spill will not drier while beneficial to gas by being advisable.In the utility model drier can have multiple, for example Silica.
The organic exhaust gas produced during the utility model DYE PRODUCTION are when being processed, first by organic exhaust gas via entering Feed channel 1 enter sack cleaner 4 carry out dedusting, through 4 dedusting of sack cleaner after, waste gas enter gas pipeline 3 in, due to Absorbing unit 31 is provided with conveyance conduit 3 between sack cleaner 4 and low-light resonance exhaust processor 5, therefore waste gas is at this In gas pipeline 3 during conveying, carry out preliminary decolorization adsorption and process, finally low-light resonance is entered via gas pipeline 3 Exhaust processor 4 is processed, and low-light resonance exhaust processor 4 is very strong using the effect generation oxidability of photochemical catalytic oxidation Hydroxyl radical free radical and free oxygen radical, the organic principle in oxidizing gas, using microwave high energy high-penetrability, further rupture Emission molecule chain, produces a high oxidation body (being commonly called as " plasma-based "), and high oxidation body one kind is higher by more than 2000 than ozone oxidation ability Times oxysome, can be by the organic matter exhaustive oxidation in waste gas into H2O and CO2.
After waste gas of the present utility model carries out oxidation processes in low-light resonance exhaust processor 4, via gas pipeline 3 Entering in spray column 5 carries out Water spray process, for sloughing the unstable ozone in part, the taste of gas is removed.As water sprays After pouring, in waste gas may remnant steam, when the waste gas after the utility model deodorization is discharged via discharge duct 2, Can be dried via the drying unit 21 in discharge duct 2, finally discharge via discharge duct 2.

Claims (4)

1. a kind of organic waste gas treatment system, including admission line and discharge duct, it is characterised in that also include by appendix Sack cleaner and spray column that road is sequentially connected, the admission line is connected with the air inlet of sack cleaner, described Discharge duct is connected with the gas outlet of spray column, is provided with least one drying unit in the discharge duct.
2. organic waste gas treatment system as claimed in claim 1, it is characterised in that the drying unit is for being filled with drier Dry cavity, this dries cavity two side walls consistent with gas flow and is the gas permeation net that supplied gas are passed through.
3. organic waste gas treatment system as claimed in claim 1, it is characterised in that the discharge duct is helix tube.
4. organic waste gas treatment system as claimed in claim 1, it is characterised in that the admission line is helix tube.
CN201620744049.2U 2016-07-11 2016-07-11 A kind of organic waste gas treatment system Expired - Fee Related CN206008465U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620744049.2U CN206008465U (en) 2016-07-11 2016-07-11 A kind of organic waste gas treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620744049.2U CN206008465U (en) 2016-07-11 2016-07-11 A kind of organic waste gas treatment system

Publications (1)

Publication Number Publication Date
CN206008465U true CN206008465U (en) 2017-03-15

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107376637A (en) * 2017-08-03 2017-11-24 成都漆彩之星环保科技有限公司 Containing the lacquer spraying waste gas processing unit by photooxidation catalysis system
CN108619901A (en) * 2017-03-23 2018-10-09 上海赜羽环保技术有限公司 Two butyryl house exhaust treatment process
CN112121638A (en) * 2020-09-30 2020-12-25 威海海洋职业学院 Ship tail gas washing tower with direct discharging function

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108619901A (en) * 2017-03-23 2018-10-09 上海赜羽环保技术有限公司 Two butyryl house exhaust treatment process
CN107376637A (en) * 2017-08-03 2017-11-24 成都漆彩之星环保科技有限公司 Containing the lacquer spraying waste gas processing unit by photooxidation catalysis system
CN112121638A (en) * 2020-09-30 2020-12-25 威海海洋职业学院 Ship tail gas washing tower with direct discharging function

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170315

Termination date: 20210711

CF01 Termination of patent right due to non-payment of annual fee