CN107185393A - Industrial VOC processing systems - Google Patents
Industrial VOC processing systems Download PDFInfo
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- CN107185393A CN107185393A CN201710497278.8A CN201710497278A CN107185393A CN 107185393 A CN107185393 A CN 107185393A CN 201710497278 A CN201710497278 A CN 201710497278A CN 107185393 A CN107185393 A CN 107185393A
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- Prior art keywords
- voc
- nutrient solution
- cracking case
- processing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/95—Specific microorganisms
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/12—Methods and means for introducing reactants
- B01D2259/124—Liquid reactants
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
The present invention provides a kind of industrial VOC processing systems, including the first processing segment structure, second processing segment structure, sensing detection device and MICROCOMPUTER PROCESSING center, first processing segment structure is using cracking enzyme solutions circulated sprinkling structure, second processing segment structure circulates foster microbial structure using microbial nutrient solution, sensing detection device includes two detectors, it is separately positioned on the port of export and the port of export of gas, to detect the content of organic gas and send MICROCOMPUTER PROCESSING center to, compare the proportion of port of export organic gas content and arrival end organic gas in real time in MICROCOMPUTER PROCESSING center.VOC air treatment systems of the present invention using cracked solution combination microorganism nibble bite removing VOC by the way of, the VOC in VOC air can effectively be removed, and the utilization structure of circulation is provided with, utilizing status is improved, and lysate or nutrient solution can be supplemented in time.
Description
Technical field
The present invention relates to the environmental protection equipment for administering Organic Waste Gas Pollution, more particularly to a kind of industrial VOC processing systems.
Background technology
VOC materials refer to the general name of volatile organic matter under normal temperature, common are formaldehyde, toluene, dimethylbenzene, acetone and fourth
Ketone etc..In the industries such as petrochemical industry, pharmacy, paint, coating, electronic manufacture, surface anticorrosion, shoemaking, printing and communications and transportation
Production and use during can produce substantial amounts of VOC, extreme influence is caused to air quality, VOC has stimulation to human body
And to the toxic effect of human body viscera, be detrimental to health, and VOC is inflammable causes potential safety hazard, and VOC is because discharge capacity is big, plant
Class is more, difficult degradation, strong toxicity, potential safety hazard have become greatly focus of the current whole world various countries to air-treatment problem.
Administering the major technique of volatile organic compounds pollution at present has：Be catalyzed burning, charcoal absorption, low temperature etc. from
Son, ultraviolet light etc..Catalytic combustion technology treatment effect ratio more thoroughly, but needs higher organic exhaust gas concentration, generally
The concentration of organic exhaust gas does not all reach the requirement of burning, it is necessary to use the auxiliary combustions such as natural gas, this method construction and operation
Cost is all higher.Adsorption effect of activated carbon in water is also more satisfactory, but the activated carbon cost that places one's entire reliance upon is high, and can not effectively supervise
Replacing construction is controlled, can only regularly replace, cause cost to waste sometimes.Low-temperature plasma and ultraviolet light are gone to organic exhaust gas
Except rate is less desirable.
The content of the invention
In view of the above, present invention research and development are a kind of is different from traditional industrial VOC processing systems, can effectively remove industry
VOC in gas, improves and removes VOC utilization rate of raw materials, to save production cost, while can realize timely except VOC raw material
Supplement is changed.
The technical scheme that the present invention is provided is：A kind of industrial VOC processing systems, including the first processing segment structure, at second
Segment structure, sensing detection device, MICROCOMPUTER PROCESSING center and blower fan are managed, the first processing segment structure is used to remove dust and VOC is big
Molecule, second processing segment structure is used to remove VOC small molecules, and fan action is in gas so that gas sequentially passes through the first processing
Segment structure and second processing segment structure, the first processing segment structure include the first body, are arranged on the spray on top in the first body
Be equipped with lyases solution in device and the cracking case being arranged on below the first body, cracking case, cracking case by pipeline with
First body is connected so that the solution in the first body is flowed into cracking case, and cracking case is connected by pipeline with spray equipment, is split
The first water pump is provided with solution case so that the solution cracked in case is delivered into spray equipment incessantly, the first body implosion is realized
Solve the circulated sprinkling of enzyme solutions；Second processing segment structure includes the second body, and some micro- lifes in the second body are arranged in succession
Thing enzymolysis device and the nutrient solution service tank being built up in below the second body, microorganism enzymolysis device include both ends open insertion
Casing, set up some rotatable columns in casing, column periphery is formed with the microorganism that VOC gases are bitten for nibbling, case
The top of body is provided with liquid storage cylinder and connected with column gap, is penetrated into for the nutrient solution of liquid storage cylinder to column, so as to carry
For the nutrition supply to microorganism, nutrient solution service tank is connected for the nutrient solution in the second body by pipeline with the second body
Flow into nutrient solution service tank, while nutrient solution service tank is connected with liquid storage cylinder, the second water pump be provided with nutrient solution service tank,
So that the nutrient solution timing in nutrient solution service tank is delivered into liquid storage cylinder, recycling for nutrient solution in the second body is realized, is passed
Feeling detection means includes the first detector and the second detector, and the first detector is arranged on the arrival end of the first body, to detect
VOC content and MICROCOMPUTER PROCESSING center is sent at arrival end, the second detector is arranged on the port of export of the second body, to examine
Survey the port of export at VOC content and send MICROCOMPUTER PROCESSING center to.
Further, first body is double-layer structure, and top layer equally spacedly installs spray equipment, the spray of spray equipment
Head is extended downwardly into bottom, and the bottom supplied gas of the first body is passed through.
Further, the bottom surface of first body or the second body is set to inclined plane.
Further, active carbon layer is set in first body.
Further, some baffle plates are set in the cracking case, and top surface of the baffle plate in cracking case is arranged alternately with bottom surface,
Wherein, the baffle plate for being connected to cracking case top surface is isometric, and the spacing between cracking case inner bottom surface is equal, is connected to bottom in cracking case
The height of baffle plate in face is reduced one by one from a lateral opposite side of cracking case.
Further, filter screen is set in the cracking case.
Further, second body is in double-layer structure up and down, and upper strata is used as the circulation passage of enzyme bacterial nutrient solution, lower floor
Some drip hole are offered between the space bar of the ecological enzymolysis device of installation, upper strata and lower floor.
Further, the periphery on the casing top has protruded out flange upwards, is correspondingly formed the liquid storage cylinder.
Further, enzyme bacterium set is arranged with the column, enzyme bacterium is put with microbial inoculant coating.
Further, the ratio of port of export VOC content and arrival end VOC content is compared at the MICROCOMPUTER PROCESSING center in real time,
When the ratio of port of export VOC content and arrival end VOC content is more than a certain preset value, then nutrition is injected toward nutrient solution service tank
Injection cracking enzyme solutions in liquid and/or past cracking case.
Beneficial effects of the present invention, VOC air treatment systems of the present invention are nibbled using cracked solution combination microorganism and bite removing
VOC mode, can effectively remove the VOC in VOC air, and be provided with the utilization structure of circulation, improve utilizing status, and
And lysate or nutrient solution can be supplemented in time.
Brief description of the drawings
Described above is only the general introduction of technical solution of the present invention, in order to illustrate more clearly of technical scheme, under
Face will be briefly described to the accompanying drawing used required in embodiment or description of the prior art, and the accompanying drawing in description is only pair
Should in the present invention specific embodiment, to those skilled in the art, on the premise of not paying creative work,
Other accompanying drawings can also be obtained according to these accompanying drawings when needing.
Fig. 1 is the structural principle sketch of industry VOC processing systems of the invention；
Fig. 2 is the principle schematic diagram of present pre-ferred embodiments industry VOC processing systems；
Fig. 3 is the structural representation of the second body of industry VOC the second pipeline sections of processing system of the invention；
Fig. 4 is the structural representation of the ecological enzymolysis device in industry VOC the second bodys of processing system of the invention；
Fig. 5 is the structural representation of the enzyme bacterium set of industry VOC processing systems of the invention；
Fig. 6 is the structural representation that present pre-ferred embodiments industry VOC processing systems are applied.
Embodiment
In order to elaborate the technical scheme that the present invention is taken to reach predetermined technique purpose, below in conjunction with this hair
Accompanying drawing in bright embodiment, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described
Embodiment is only the section Example of the present invention, rather than whole embodiments, also, before creative work is not paid
Put, the technological means or technical characteristic in embodiments of the invention can be replaced, below with reference to the accompanying drawings and in conjunction with the embodiments
To describe the present invention in detail.
Referring to Fig. 1, a kind of industrial VOC processing systems, including mobile air-breathing arm assembly and gas-handling configurations, it is mobile
Air-breathing arm assembly draw gas, and deliver the gas to gas-handling configurations, gas-handling configurations are by the VOC processing in gas.
Mobile air-breathing arm assembly includes air-suction cover 11, the mobile swing arm 12 being connected with air-suction cover 11 and is connected to air-breathing
Cover the airway tube 13 of 11 ends.Air-suction cover 11 may be provided at the top of industrial flow-line or workbench or exhaust air discharge equipment, with
The pernicious gases such as draw gas, are such as arranged on the top of dispensing station to draw the penetrating odor that glue is emitted, are arranged on
The top of forming machine, to draw the waste gas produced during forming machine shaping.Mobile one end of swing arm 12 is hinged on the tail end of air-suction cover 11, separately
One end is hinged on a column, and mobile swing arm 12 is swung with respect to column, drives air-suction cover 11 to swing, the one end of airway tube 13 is hinged on
On air-suction cover 11, the other end is connected and is hinged on the pipeline of gas-handling configurations, realizes that the gas for drawing air-suction cover 11 is defeated
Deliver in gas-handling configurations.
Gas-handling configurations include the first processing segment structure 21, second processing segment structure 22, sensing detection device 23, microcomputer
Processing center (not shown) and blower fan 24.Referring to Fig. 2, the first processing segment structure 21 is used to remove dust and VOC macromoleculars,
First processing segment structure 21 includes the first body 211, be arranged in the first body 211 the spray equipment (not shown) on top and
It is arranged on the cracking case 212 of the lower section of the first body 211.Specifically, the first body 211 can be double-layer structure, and top layer is equally spacedly
Spray equipment is installed, the shower nozzle of spray equipment is extended downwardly into bottom, the bottom supplied gas of the first body 211 is passed through.In gas
When body passes through, it can be landed by the dust and VOC macromoleculars opened in spray equipment, gas by spraying, flow into cracking case
In 212, VOC macromoleculars will be cracked in cracking case 212.Cracking case 212, the first pipe are flowed into for the ease of the liquid after spray
The bottom surface of body 211 is set to inclined plane, is flowed into order to which liquid collects in cracking case 212.Inclined plane can be along the one of body
End, which has a down dip, extends to a surface of other end formation, or at the two ends of body respectively with respect to collecting after having a down dip, substantially in inversion
"eight" shape outlet of confluxing, inclined plane relative to the inclination angle of the formation of cracking case 212 bottom surface preferably select for 15 °-
20°.Further, in order to improve abundant sedimentation of the spray to VOC macromoleculars, active carbon layer is set in the first body 211
213, the absorption when gas passes through by active carbon layer 213 to VOC gases, and fallen into by spray to cracking case 212, can
Fully VOC macromoleculars are fallen into cracking case 212.Lyases solution is equipped with cracking case 212, such as cracking aromatic hydrocarbon etc.
Crack enzyme solutions.
The side of cracking case 212 is provided with the first connecting tube 201 and is connected with the manifold port of the first body 211 so that first
Solution in body 211 is flowed into cracking case 212, while the opposite side for cracking case 212 is provided with the second connecting tube 202 and spray
Device is connected, to supply cracking enzyme solutions to spray equipment.The first water pump 214 is provided with cracking case 212, case 212 will be cracked
Interior solution is delivered to spray equipment incessantly, and the circulation spray of the cracking enzyme solutions of the first processing segment structure 21 so can be achieved
Drench.
In order to improve lysis efficiency of the VOC macromoleculars in cracking case 212, some baffle plates will be set in cracking case 212
215, top surface of the baffle plate 215 in cracking case is arranged alternately with bottom surface, wherein, it is connected to baffle plate 215 of the cracking top surface of case 212 etc.
Long, the spacing between the cracking inner bottom surface of case 212 is equal, is connected to the height of baffle plate of the cracking inner bottom surface of case 212 from provided with second
The side of one lateral first connecting tube of connecting tube is reduced one by one, and the spacing between the cracking inner top surface of case 212 becomes larger, such as
This, the solution that the first connecting tube 201 enters in cracking case 212 does corrugated stream from the side of cracking case 212 to opposite side
It is dynamic, and because the baffle plate for being connected to the cracking inner bottom surface of case 212 is reduced step by step so that solution can automatic overflow, being detained, VOC is big
Extend its flow path while molecule, can be fully by VOC macromolecular cleavages.In addition, being set in the front end for entering cracking case 212
Filter screen 216, can filter out dust.
In addition, with the extension of use time, because the gas flowing entered in the first body 211 can blow away part cracking
The active ingredient of enzyme solutions and the cracking enzyme solutions used is reduced, and cracking case 212, which is connected with, is automatically replenished cracking enzyme solutions
Liquid supply device (diagram is shown) and by MICROCOMPUTER PROCESSING center control start, MICROCOMPUTER PROCESSING center analysis to need add crack
During enzyme solutions, then start default height in toward cracking case 212 injection lysate to cracking case 212.
Second processing segment structure 22 passes through for handling the gas of segment structure 21 by first, to remove the VOC in gas
Small molecule, second processing segment structure 22 include the second body 221, be built up in the ecological enzymolysis device 30 in the second body 221 with
And it is built up in the enzyme bacterial nutrient solution service tank 223 of the lower section of the second body 221.Referring to Fig. 3, the second body 221 can be in up and down two
Rotating fields, upper strata is as the circulation passage of enzyme bacterial nutrient solution, and lower floor installs ecological enzymolysis device 30, also, upper strata and lower floor
Some drip hole are offered between space bar, so that the enzyme bacterial nutrient solution on upper strata is instilled into ecological enzymolysis device 30.With the first pipe
The fabric of body 211, the bottom surface of the second body 221 is set to inclined plane, and enzyme bacterium is flowed into order to which enzyme bacterial nutrient solution collects
In nutrient solution service tank 223.
Ecological enzymolysis device 30 is several, in the lower floor for being arranged in the second body 221.Fig. 4 and Fig. 5 is referred to,
Ecological enzymolysis device 30 includes the casing 31 of both ends open insertion, is built up in the column 32 in casing 31, and be set in column
32 enzyme bacterium set 33.The opposite end insertion of casing 31 is for airflow, and the periphery on the top of casing 31 has protruded out flange upwards, right
Ground is answered to form a liquid storage cylinder 34, liquid storage cylinder 34 connects the nutrient solution dripped from the upper strata of the second body 221 to hold, and column 32 is built up in
In the casing 31 and top of column 32 passes from the top surface of casing 31 and entered in liquid storage cylinder 34 so that the enzyme bacterium in liquid storage cylinder 34
Nutrient solution can be down penetrated into along column 32 to one section be located in casing 31 of column 32.Setting of the column 32 in casing 31
It can also be arranged in matrix arrangements in quincuncial pile shape.Enzyme bacterium set 33 is set on column 32, can be rotated around column 32.Enzyme bacterium set 33
Upper to have microbial inoculant coating, microbial inoculant coating main component is that have the original of symbiosis to bite VOC fungies and part
Core biotic component, composition, microbial inoculant coating master of the present invention are allocated according to the gas ingredients of different pollution sources by a certain percentage
Will be using compound carbon-based nano bed (coating), enzyme bacterial nutrient solution is used to provide nutrient to the microorganism in microbial inoculant coating,
For microbial reproduction, culture.Containing trace mineral, carbohydrate and for stable and acceleration microbiologic population's generation in enzyme bacterial nutrient solution
The enzyme preparation thanked, VOC is considered as the nutriment of microorganism.Enzyme bacterial nutrient solution can be directly penetrated into enzyme along after the flow down of column 32
On bacterium set 33, so as to provide nutrient to microbial inoculant coating, for microbial reproduction, microorganism nibbles the VOC bitten in gas.Enzyme bacterium
Set 33 rotates around column 32 under the action of the forces of the wind, can be fully by nutrient solution uniform absorption.Enzyme bacterium covers the absorption of 33 pairs of nutrient solutions
When sufficient, unnecessary nutrient solution can flow into the bottom surface flowed into behind the bottom surface of casing 31 in second body 221 along column 32 and collect,
Then flow into enzyme bacterial nutrient solution service tank 223.
Enzyme bacterial nutrient solution service tank 223 is provided with the first pipeline and is connected with the manifold port of the bottom surface of the second body 221 so that the
Nutrient solution in two bodys 221 is flowed into enzyme bacterial nutrient solution service tank 223, and enzyme bacterial nutrient solution service tank 223 is provided with the second pipe
Road is connected with the circulation passage on the upper strata of the second body 221, so as to nutrient solution service tank 223 be connected with liquid storage cylinder 34, nutrient solution
The second water pump 224 is provided with service tank 223, the nutrient solution timing in nutrient solution service tank 223 is delivered to liquid storage cylinder 34,
Realize recycling for nutrient solution in the second body 221.
With the extension of use time, because the gas flowing entered in the second body 221 can blow away part nutrient solution, seek
Nutrient solution service tank 223 is connected with the liquid supply device (diagram is shown) that is automatically replenished enzyme bacterial nutrient solution solution and by MICROCOMPUTER PROCESSING
Heart control starts, and in MICROCOMPUTER PROCESSING center analysis to when needing to add enzyme bacterial nutrient solution, then starts and is injected toward nutrient solution service tank
Default height in nutrient solution to nutrient solution service tank 223.It is appreciated that preset height can pass through electromagnetic induction control or floating
Valve is controlled.
Sensing detection device 23 includes the first detector 231 and the second detector 232, and the first detector 231 is arranged on the
The arrival end of one body 211, to detect at the arrival end in gas the content of organic gas and send MICROCOMPUTER PROCESSING center to,
Second detector 232 is arranged on the port of export of the second body 221, with detect at the port of export in gas the content of organic gas and
Send MICROCOMPUTER PROCESSING center to.
The proportion of port of export organic gas content and arrival end organic gas is compared at MICROCOMPUTER PROCESSING center in real time, when going out
When mouth end organic gas content and the ratio of arrival end organic gas are more than a certain preset value, then VOC fails to reach that removing is required,
Then nutrient solution or lyases are bitten except efficiency is not up to requirement, start toward nutrient solution service tank 223 and inject nutrient solution and/or toward splitting
Solve supplement cracking enzyme solutions in case 212.
Blower fan 24 is preferably disposed on the port of export of the second body 221 and preferably in the front end of the second detector 232, passed through
The effect of blower fan 24 so that gas sequentially passes through the first processing segment structure and second processing segment structure.
It is appreciated that in order to fully effectively remove VOC, the quantity of the first processing segment structure 21 and second processing segment structure 22
It can set as needed.
Referring to Fig. 6, industry VOC processing systems are applied in industrial production workshop, some mobile air suction arm dresses can be set
Some VOC gases of the correspondence of air-suction cover 11 put distribute station or some VOC gas discharging apparatus, by one first processing section
After structure 21, then by two second processing segment structures 22, into blower fan 24, then collect and discharged from a total exhaust duct 41.
The quantity of first detector 231 correspondence air-suction cover 11 is arranged on the arrival end of every one first body 211, the second 232 pairs of detector
The port of export of every one second body 221 should be arranged on, and the first detector 231 and the second detector 232 are connected to a number
According to carrying case 42, to be sent to MICROCOMPUTER PROCESSING center.Cracking case 212 is provided toward the spray equipment on top in the first body 211 to be split
Solve liquid；Enzyme bacterial nutrient solution service tank 223 is toward the ecological enzymolysis device 30 in the second body 221 of two second processing segment structures 22
Nutrient solution is provided.
To sum up, VOC air treatment systems of the present invention nibble the side bitten and remove VOC using cracked solution combination microorganism
Formula, can effectively remove the VOC in VOC air, and be provided with the utilization structure of circulation, improve utilizing status, and can and
When supplement lysate or nutrient solution.
The above described is only a preferred embodiment of the present invention, any formal limitation not is made to the present invention, though
So the present invention is disclosed above with preferred embodiment, but is not limited to the present invention, any to be familiar with this professional technology people
Member, without departing from the scope of the present invention, when the technology contents using the disclosure above make a little change or modification
For the equivalent embodiment of equivalent variations, as long as be without departing from technical solution of the present invention content, according to the technical spirit of the present invention,
Within the spirit and principles in the present invention, any simple modification, equivalent substitution and improvement for being made to above example etc., still
Belong within the protection domain of technical solution of the present invention.
Claims (10)
1. a kind of industrial VOC processing systems, including the first processing segment structure, second processing segment structure, sensing detection device, microcomputer
Processing center and blower fan, the first processing segment structure are used to remove dust and VOC macromoleculars, and second processing segment structure is used to remove
VOC small molecules, fan action is in gas so that gas sequentially passes through the first processing segment structure and second processing segment structure, and it is special
Levy and be：First processing segment structure includes the first body, is arranged in the first body the spray equipment on top and is arranged on the
Be equipped with lyases solution in cracking case below one body, cracking case, cracking case by pipeline be connected with the first body for
Solution in first body is flowed into cracking case, and cracking case is connected by pipeline with spray equipment, and first is provided with cracking case
Water pump realizes the circulation spray of cracking enzyme solutions in the first body so that the solution cracked in case is delivered into spray equipment incessantly
Drench；Second processing segment structure includes the second body, some microorganism enzymolysis devices being arranged in succession in the second body and sets
The nutrient solution service tank stood in below the second body, microorganism enzymolysis device includes setting in the casing of both ends open insertion, casing
Vertical to have some rotatable columns, column periphery is formed with the microorganism that VOC gases are bitten for nibbling, and the top of casing is provided with storage
Sap cavity and connect, penetrated into for the nutrient solution of liquid storage cylinder to column, so as to provide the nutrition to microorganism with column gap
Supply, nutrient solution service tank is connected so that the nutrient solution in the second body flows into nutrient solution service tank by pipeline with the second body
It is interior, while nutrient solution service tank is connected with liquid storage cylinder, the second water pump is provided with nutrient solution service tank, by nutrient solution service tank
Interior nutrient solution timing is delivered to liquid storage cylinder, realizes recycling for nutrient solution in the second body, and sensing detection device includes the
One detector and the second detector, the first detector are arranged on the arrival end of the first body, to detect the content of VOC at arrival end
And MICROCOMPUTER PROCESSING center is sent to, the second detector is arranged on the port of export of the second body, to detect containing for VOC at the port of export
Measure and send MICROCOMPUTER PROCESSING center to.
2. industrial VOC processing systems according to claim 1, it is characterised in that：First body is double-layer structure, top
Layer equally spacedly installs spray equipment, and the shower nozzle of spray equipment is extended downwardly into bottom, the bottom supplied gas warp of the first body
Cross.
3. industrial VOC processing systems according to claim 1, it is characterised in that：First body or the second body
Bottom surface is set to inclined plane.
4. industrial VOC processing systems according to claim 1, it is characterised in that：Activated carbon is set in first body
Layer.
5. industrial VOC processing systems according to claim 1, it is characterised in that：Some baffle plates are set in the cracking case,
Top surface of the baffle plate in cracking case is arranged alternately with bottom surface, wherein, the baffle plate for being connected to cracking case top surface is isometric, in cracking case
Spacing between bottom surface is equal, and the height of baffle plate for being connected to cracking case inner bottom surface drops one by one from a lateral opposite side of cracking case
It is low.
6. industrial VOC processing systems according to claim 5, it is characterised in that：Filter screen is set in the cracking case.
7. industrial VOC processing systems according to claim 1, it is characterised in that：Second body is in two layers of knot up and down
Structure, upper strata is as the circulation passage of enzyme bacterial nutrient solution, and lower floor installs ecological enzymolysis device, opened up between the space bar of upper strata and lower floor
There are some drip hole.
8. industrial VOC processing systems according to claim 1, it is characterised in that：The periphery on the casing top is convex
Stretching has flange, is correspondingly formed the liquid storage cylinder.
9. industrial VOC processing systems according to claim 1, it is characterised in that：Enzyme bacterium set, enzyme are arranged with the column
Bacterium is put with microbial inoculant coating.
10. industrial VOC processing systems according to claim 1, it is characterised in that：Compare in real time at the MICROCOMPUTER PROCESSING center
The ratio of port of export VOC content and arrival end VOC content, when the ratio of port of export VOC content and arrival end VOC content is more than certain
During one preset value, then inject nutrient solution toward nutrient solution service tank and/or crack enzyme solutions toward injection in cracking case.
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| CN201710497278.8A CN107185393A (en) | 2017-06-26 | 2017-06-26 | Industrial VOC processing systems |
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| CN201710497278.8A CN107185393A (en) | 2017-06-26 | 2017-06-26 | Industrial VOC processing systems |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108362851A (en) * | 2018-01-31 | 2018-08-03 | 河南工程学院 | A kind of experimental method and device using the distinguished and admirable gas of microbial degradation coal mine |
| CN114053864A (en) * | 2021-12-15 | 2022-02-18 | 青岛万慧源环保科技有限公司 | Treatment method of waste gas containing organic pollutants |
Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2310067Y (en) * | 1997-09-15 | 1999-03-10 | 徐忠 | Self-cleaning domestic sewage purifier |
| US6461510B1 (en) * | 1999-07-23 | 2002-10-08 | Tennessee Valley Authority | High-efficiency processes for destruction of contaminants |
| CN1974435A (en) * | 2006-12-11 | 2007-06-06 | 上海市莘庄工业区经济技术发展有限公司 | Biological package treatment method for draining port in river |
| CN1986738A (en) * | 2005-12-23 | 2007-06-27 | 张才腾 | Combined oil-metal polymer solution and its application |
| CN102504994A (en) * | 2011-12-19 | 2012-06-20 | 南宁纵联科技有限公司 | Method for preparing fructooligosaccharide by using baffled bioreactor |
| CN202398267U (en) * | 2011-12-30 | 2012-08-29 | 上海安居乐环保科技有限公司 | Novel spray-painting waste gas treating device |
| CN202823128U (en) * | 2012-02-14 | 2013-03-27 | 兰州红菌生物技术有限责任公司 | Hydrogen sulfide removing device with filter |
| CN103055695A (en) * | 2011-10-19 | 2013-04-24 | 郑承煜 | Waste gas purification method and device |
| CN104587817A (en) * | 2014-12-03 | 2015-05-06 | 曾玉成 | VOC decomposition composite-purifying processing apparatus and method |
| CN105540995A (en) * | 2015-12-03 | 2016-05-04 | 南京师范大学 | Ecological utilization method for purifying rural household sewage and sewage generated by aquatic bird breeding |
| CN105727741A (en) * | 2016-04-20 | 2016-07-06 | 张尧 | Air treatment box and air treatment equipment system used for production line |
| CN106000083A (en) * | 2016-07-27 | 2016-10-12 | 张尧 | Bio-enzyme device and VOC (Volatile Organic Compounds) gas treating system with same |
| CN207085673U (en) * | 2017-06-26 | 2018-03-13 | 佛山瀚兽环境科技服务有限公司 | Industrial VOC processing systems |
-
2017
- 2017-06-26 CN CN201710497278.8A patent/CN107185393A/en active Pending
Patent Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2310067Y (en) * | 1997-09-15 | 1999-03-10 | 徐忠 | Self-cleaning domestic sewage purifier |
| US6461510B1 (en) * | 1999-07-23 | 2002-10-08 | Tennessee Valley Authority | High-efficiency processes for destruction of contaminants |
| CN1986738A (en) * | 2005-12-23 | 2007-06-27 | 张才腾 | Combined oil-metal polymer solution and its application |
| CN1974435A (en) * | 2006-12-11 | 2007-06-06 | 上海市莘庄工业区经济技术发展有限公司 | Biological package treatment method for draining port in river |
| CN103055695A (en) * | 2011-10-19 | 2013-04-24 | 郑承煜 | Waste gas purification method and device |
| CN102504994A (en) * | 2011-12-19 | 2012-06-20 | 南宁纵联科技有限公司 | Method for preparing fructooligosaccharide by using baffled bioreactor |
| CN202398267U (en) * | 2011-12-30 | 2012-08-29 | 上海安居乐环保科技有限公司 | Novel spray-painting waste gas treating device |
| CN202823128U (en) * | 2012-02-14 | 2013-03-27 | 兰州红菌生物技术有限责任公司 | Hydrogen sulfide removing device with filter |
| CN104587817A (en) * | 2014-12-03 | 2015-05-06 | 曾玉成 | VOC decomposition composite-purifying processing apparatus and method |
| CN105540995A (en) * | 2015-12-03 | 2016-05-04 | 南京师范大学 | Ecological utilization method for purifying rural household sewage and sewage generated by aquatic bird breeding |
| CN105727741A (en) * | 2016-04-20 | 2016-07-06 | 张尧 | Air treatment box and air treatment equipment system used for production line |
| CN106000083A (en) * | 2016-07-27 | 2016-10-12 | 张尧 | Bio-enzyme device and VOC (Volatile Organic Compounds) gas treating system with same |
| CN207085673U (en) * | 2017-06-26 | 2018-03-13 | 佛山瀚兽环境科技服务有限公司 | Industrial VOC processing systems |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108362851A (en) * | 2018-01-31 | 2018-08-03 | 河南工程学院 | A kind of experimental method and device using the distinguished and admirable gas of microbial degradation coal mine |
| CN114053864A (en) * | 2021-12-15 | 2022-02-18 | 青岛万慧源环保科技有限公司 | Treatment method of waste gas containing organic pollutants |
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