CN206008420U - Organic exhaust gas multistep treatment purifier - Google Patents
Organic exhaust gas multistep treatment purifier Download PDFInfo
- Publication number
- CN206008420U CN206008420U CN201620974819.2U CN201620974819U CN206008420U CN 206008420 U CN206008420 U CN 206008420U CN 201620974819 U CN201620974819 U CN 201620974819U CN 206008420 U CN206008420 U CN 206008420U
- Authority
- CN
- China
- Prior art keywords
- exhaust gas
- organic exhaust
- oxygen
- degraded pond
- packed tower
- 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
Links
- 239000007921 spray Substances 0.000 claims abstract description 48
- 239000007789 gas Substances 0.000 claims abstract description 46
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 35
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 35
- 238000010521 absorption reaction Methods 0.000 claims abstract description 31
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 31
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 29
- 239000001301 oxygen Substances 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 238000005273 aeration Methods 0.000 claims abstract description 25
- 238000013019 agitation Methods 0.000 claims abstract description 25
- 239000003610 charcoal Substances 0.000 claims abstract description 23
- 238000011049 filling Methods 0.000 claims abstract description 18
- 238000001914 filtration Methods 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims description 21
- 239000000945 filler Substances 0.000 claims description 7
- 238000005507 spraying Methods 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 4
- 241000628997 Flos Species 0.000 claims description 3
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 238000000746 purification Methods 0.000 abstract description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 18
- 238000000034 method Methods 0.000 description 16
- 230000008569 process Effects 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- 150000002894 organic compounds Chemical class 0.000 description 9
- 239000010815 organic waste Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 5
- 239000008187 granular material Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000000813 microbial effect Effects 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 239000012855 volatile organic compound Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- QRSFFHRCBYCWBS-UHFFFAOYSA-N [O].[O] Chemical compound [O].[O] QRSFFHRCBYCWBS-UHFFFAOYSA-N 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000010796 biological waste Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- OKTJSMMVPCPJKN-BJUDXGSMSA-N carbon-11 Chemical compound [11C] OKTJSMMVPCPJKN-BJUDXGSMSA-N 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 210000003850 cellular structure Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007850 degeneration Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- RXKJFZQQPQGTFL-UHFFFAOYSA-N dihydroxyacetone Chemical compound OCC(=O)CO RXKJFZQQPQGTFL-UHFFFAOYSA-N 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000005662 electromechanics Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of organic exhaust gas multistep treatment purifier, including spray packed tower (4), absorb degraded pond (12), circulating pump (20), absorb liquid storage tank (21), described absorption degraded pond (12) includes aeration agitation part and multistage filtering part, the absorption degraded pond (12) of aeration agitation part is provided with the upper division board (15) that bottom communicates, and saturation powdered carbon (11) swims in aeration agitation and partially absorbs above liquid；The absorption degraded pond (12) of multistage filtering part is provided with least two grades modularity screen frames (18), modularity screen frame (18) and is placed with charcoal filling silk screen basket (17) that can be exchanged；The oxygen feeder (7) that the entrance point of described spray packed tower (4) is connected with powdered carbon charge door (8) and is connected with source of oxygen (10), organic exhaust gas, powdered carbon and oxygen mix enter spray packed tower (4).Using after this said structure, with simple and reasonable, easy for operation, operating cost low, safety and stability is good, purification efficiency is high the features such as.
Description
Technical field
This utility model is related to organic waste-gas purification technical field, and particularly one kind is carried out to organic exhaust gas using charcoal and oxygen
The purifier of multistep treatment.
Background technology
All product surface must be entered in industries such as furniture, shoemaking, automobile, machinery, household electrical appliances, electromechanics, plastic, five metals
Row is processed, most effective at present and most efficiently method is exactly to process to produce motley product by painted surface, can be with
Greatly improve the aesthetic feeling of product.But release of volatilizing in paint production, dilution, spraying process and during subsequent cure has
Machine exhaust emission.The comparison of ingredients of Organic Waste Gas Pollution thing is complicated, mainly has low-molecular-weight organic compound and macromolecule organic
Compound, the water solublity of height organic compound and degradability differ greatly, particularly as surface spraying, plastic processing, chemical industry,
The organic exhaust gas of the generations such as rubber, pharmacy, chemical fertilizer, printing, weaving, the solvent and diluent of surface spraying have benzene, toluene, diformazan
Benzene etc. is insoluble in the stronger water of polarity, and benzene,toluene,xylene is non-polar high polymer organic compound material, also has readily soluble water
The low pole low-molecular-weight organic compound such as methanol, ethanol, acetone, aliphatic ketone, formaldehyde, acetaldehyde.
At present to VOCs treatment also without preferable method, the more commonly used method is to utilize microbial technology
To reach clean-up effect.The method by the use of microorganism using waste gas in organic component as its vital movement the energy or other support
Point, through metabolic degradation, it is converted into simple inorganic matters CO2, water etc. and cell component.External since the eighties, start
Industrial waste gas is processed with biotechnology, technology is cleaned, easy to operate, can be carried out at normal temperatures and pressures reacting, especially
Which have received good effect on low concentration, the waste gas purification of high flow capacity, and biological waste gas purification is the new technique of " green ".Mesh
In front biological treatment, because being affected by factors such as microbial bacteria, bio-film colonization, air quantity, humidity, temperature, the time of staying, pressure,
The problems such as easily degeneration of generation filtrate and biofilm, microbial activity reduce, the short-circuit flow for causing air film to contact, so that organic
The purification efficiency of exhaust emission reduces.Additionally, the water solublity and biological degradability to organic pollution requires also higher, biology
The startup of reactor, microbial acclimation, processing procedure persistent period, and the specific surface area of filler are few, porosity is few, ventilation resistance
Power is greatly the subject matter of current filler.The less effective of filler causes bacterial activity to reduce, equipment volume is huge, the time of staying
Long, easy blocking, affects mass transfer effect, makes filler service life short, and then directly affect the operating cost of whole system.For
This, many manufacturers and knowledgeable people exclusively carry out exploitation and develop, but not yet have comparatively ideal product to emerge so far.
Utility model content
In order to solve the problems referred to above existing for existing VOCs treatment, the purpose of this utility model is to provide a kind of knot
The organic exhaust gas that structure advantages of simple, easy for operation, operating cost are low, safety and stability is good, purification efficiency is high are multistage
Treatment and purification device.
This utility model solves the technical scheme adopted by its technical problem, it include spray packed tower, absorb degraded pond,
Circulating pump, absorption liquid storage tank, the organic exhaust gas import of spray packed tower are connected with organic exhaust gas induced duct, the row of spray packed tower
Put mouth to be connected with delivery pipe, the spray packed tower is connected with degraded pond is absorbed, spray packed tower, absorption degraded pond and circulating pump
Composition absorbing liquid loop structure；Described absorption degraded pond includes aeration agitation part and multistage filtering part, aeration agitation portion
The absorption degraded pond that divides is provided with the upper division board that bottom communicates, and saturation powdered carbon swims in aeration agitation and partially absorbs the upper of liquid
Face；The absorption degraded pond of multistage filtering part is provided with least two grades modularity screen frames, and being placed with modularity screen frame can
With the charcoal filling silk screen basket that exchanges；The entrance point of described spray packed tower is connected with powdered carbon charge door and is connected with source of oxygen
Oxygen feeder, organic exhaust gas, powdered carbon and oxygen mix enter spray packed tower, and organic exhaust gas absorb absorption in spray packed tower
On carbon filling material layer, absorbed in degraded pond with spray liquid backflow by the Organic Waste Gas Pollution material that powdered carbon absorbs absorption.
Further scheme of the present utility model, at least provided with two grades of interconvertible modules on the tower body of the spray packed tower
Change stuffing frame, on modularity stuffing frame, be placed with carbon filling material layer, spray packed tower is provided with for absorbing liquid spray head and demisting
Device；Described circulating pump one end is connected with degraded pond is absorbed, and the other end is connected with absorbing liquid spray head by connecting tube.
Further scheme of the present utility model, the both sides of described upper division board are correspondingly provided with first be connected with source of oxygen
Aeration agitation pipe and the second aeration agitation pipe.
Further scheme of the present utility model, the absorption degraded pond of the modularity screen frame outlet side are provided with and oxygen
The 3rd aeration agitation pipe that source is connected.
Further scheme of the present utility model, described source of oxygen be any one of ozone, oxygen or compressed air or
Any two kinds of mixing.
Further scheme of the present utility model, the charcoal Grain size controlling on the carbon filling material layer and charcoal filling silk screen basket is in 1-5
Between centimetre.
Further scheme of the present utility model, the powdered carbon added from powdered carbon charge door are controlled between 100-3000 mesh.
After using said structure, have the following advantages compared with the prior art and effect.
One is that the carbon filling material layer that organic exhaust gas enter spray packed tower with powdered carbon and oxygen mix carries out first order process,
Under the effect of absorbing liquid spray, Organic Waste Gas Pollution material part adsorbs on the charcoal granule of carbon filling material layer, most of absorbed liquid
Dissolving is simultaneously adsorbed by powdered carbon；The Organic Waste Gas Pollution Material recirculation of absorbing liquid and absorption on powdered carbon is dissolved in aeration agitation
Second level process is carried out in partial absorption degraded pond, further dissolving, absorption and degraded under oxygen supplement effect；Finally by suction
The modularity screen frame that receives in degraded pond carries out third level process, makes Organic Waste Gas Pollution material fill the charcoal on silk screen basket in charcoal
Further dissolving, absorption and degraded under granule effect, poisonous oxidation of organic compounds in oxidative degradation conversion process
Into nontoxic carbon dioxide and water.
Two is to enter spray packed tower due to organic exhaust gas with powdered carbon and oxygen mix, and organic exhaust gas are in spray packed tower
Molecular structure is changed by oxygen molecule catalysis oxidation, more hydroxyls, carbonyl and carboxyl not only can be formed, increase organic molecule
Polarity and hydrophilic, make Organic Waste Gas Pollution material preferably be dissolved in absorbing liquid, using the adsorptivity of charcoal, to benzene, toluene,
Dimethylbenzene carries out Filtration Adsorption absorption for non-polar high polymer organic compound material, is acted on using the adsorbent of charcoal, absorption benzene, first
The macromolecular organic compound matter such as benzene, dimethylbenzene, makes macromolecular organic compound matter be solidificated on charcoal, is filled out by clearing up replacing charcoal
The saturation charcoal granule of the bed of material and charcoal filling silk screen basket and saturation powdered carbon above absorbing liquid is swum in, then through distillation, extraction
Or burn, the useful component in organic exhaust gas is reclaimed, charcoal circulating and recovering after desorption, resource utilization are high.
Three is as the tower body of spray packed tower is using interconvertible modularity stuffing frame combinative structure, multistage filtering part
Absorption degraded pond on adopt modularity screen frame combinative structure, modularity stuffing frame and modularity screen frame increase or decrease with
And exchange is simple and convenient, same set of processing meanss can meet the requirement that different clients process different organic exhaust gas.
Four is that organic exhaust gas pass through tertiary treatment, and processing speed is fast, efficiency high, effect are good, operating cost is low.
Description of the drawings
Fig. 1 is the structural representation of the first embodiment of this utility model.
Structural representations of the Fig. 2 for second embodiment of this utility model.
Wherein, 1 floss hole, 2 demisters, 3 absorbing liquid spray heads, 4 spray packed towers, 5 carbon filling material layers, 6 modularitys are filled out
Bin, 7 oxygen feeders, 8 powdered carbon charge doors, 9 organic exhaust gas imports, 10 source of oxygen, 11 saturation powdered carbons, 12 absorb degraded pond, and 13 inhale
Liquid is received, 14 first aeration agitation pipes, division board on 15,16 second aeration agitation pipes, 17 charcoals fill silk screen basket, 18 modularity silk screens
Frame, 19 the 3rd aeration agitation pipes, 20 circulating pumps, 21 absorb liquid storage tank, 22 connecting tubes.
Specific embodiment
Shown in Fig. 1, it is a kind of the first specific embodiment of organic exhaust gas multistep treatment purifier of this utility model,
It includes spray packed tower 4, absorbs degraded pond 12, circulating pump 20, absorbs liquid storage tank 21, and described spray packed tower 4 is using vertical
Formula spraying filler tower structure, the organic exhaust gas import 9 of spray packed tower 4 are connected with organic exhaust gas induced duct, spray packed tower 4
Floss hole 1 is connected with delivery pipe, at least provided with two grades of interconvertible modularity stuffing frames 6 on the tower body of the spray packed tower 4
, carbon filling material layer 5 is placed with modularity stuffing frame 6, spray packed tower 4 is provided with for absorbing liquid spray head 3 and demister
2；20 one end of the circulating pump is connected with degraded pond 12 is absorbed, and the other end is connected with absorbing liquid spray head 3 by connecting tube 22, institute
State spray packed tower 4 and connect with degraded pond 12 is absorbed, spray packed tower 4, absorption degraded pond 12 and the composition absorbing liquid of circulating pump 20
Loop structure.The oxygen feeder that the entrance point of described spray packed tower 4 is connected with powdered carbon charge door 8 and is connected with source of oxygen 10
7, organic exhaust gas are entered in spray packed tower 4 with powdered carbon and oxygen mix, in spray packed tower 4 carry out first order process.
Described absorption degraded pond 12 includes aeration agitation part and multistage filtering part, the absorption drop of aeration agitation part
Solution pond 12 is provided with the upper division board 15 that bottom communicates, and saturation powdered carbon 11 swims in aeration agitation and partially absorbs above liquid 13；
The absorption degraded pond 12 of multistage filtering part is provided with least two grades modularity screen frames 18, is placed with modularity screen frame 18
The charcoal filling silk screen basket 17 that can be exchanged；The both sides of described upper division board 15 are correspondingly provided with the first exposure being connected with source of oxygen 10
Gas agitating pipe 14 and the second aeration agitation pipe 16.The absorption degraded pond 12 of 18 outlet side of modularity screen frame is provided with and oxygen
The 3rd aeration agitation pipe 19 that source of the gas 10 is connected.By powdered carbon adsorbs and absorbed liquid 13 dissolves Organic Waste Gas Pollution material with
Spray liquid backflow is absorbed in degraded pond 12, in the absorption degraded pond of aeration agitation part carries out second level process, is made in oxygen supplement
With lower further dissolving, absorb and degraded；Third level process is carried out finally by the modularity screen frame in degraded pond is absorbed, is made
Organic Waste Gas Pollution material fills further dissolving, absorption and degraded under the charcoal granule effect on silk screen basket in charcoal.
For the catalysis oxidation effectively to organic exhaust gas, described source of oxygen 10 is appointing for ozone, oxygen or compressed air
Meaning is a kind of or any two kinds of mixing.
For active adsorption and absorption organic exhaust gas, the charcoal granule control on the carbon filling material layer 5 and charcoal filling silk screen basket 17
System is between 1-5 centimetre.The powdered carbon added from powdered carbon charge door 8 is controlled between 100-3000 mesh.
Shown in Fig. 2, it is a kind of second specific embodiment of organic exhaust gas multistep treatment purifier of this utility model,
It is a difference in that described spray packed tower 4 using Horizental showering filler tower structure, its work with the first specific embodiment
Principle is identical with the first specific embodiment, and here is no longer repeated.
The above, simply specific embodiment of the utility model, not makes to this utility model any pro forma
Limit, on the basis of without departing from the technical solution of the utility model, done simple modification, equivalent variations or modification fall
Enter protection domain of the present utility model.
Claims (7)
1. a kind of organic exhaust gas multistep treatment purifier, including spray packed tower (4), absorbs degraded pond (12), circulating pump
(20) liquid storage tank (21), is absorbed, and the organic exhaust gas import (9) of spray packed tower (4) is connected with organic exhaust gas induced duct, and spray is filled out
The floss hole (1) of material tower (4) is connected with delivery pipe, and spray packed tower (4) are connected with degraded pond (12) is absorbed, spraying filler
Tower (4), absorption degraded pond (12) and circulating pump (20) composition absorbing liquid loop structure；It is characterized in that：Described absorption degraded pond
(12) include that aeration agitation part and multistage filtering part, the absorption degraded pond (12) of aeration agitation part are provided with bottom and communicate
Upper division board (15), saturation powdered carbon (11) swims in aeration agitation and partially absorbs above liquid；The absorption of multistage filtering part
Degraded pond (12) is provided with least two grades modularity screen frames (18), modularity screen frame (18) and is placed with the charcoal that can be exchanged
Filling silk screen basket (17)；The entrance point of described spray packed tower (4) be connected with powdered carbon charge door (8) and with source of oxygen (10)
The oxygen feeder (7) of connection, organic exhaust gas, powdered carbon and oxygen mix enter spray packed tower (4).
2. organic exhaust gas multistep treatment purifier according to claim 1, is characterized in that：Spray packed tower (4)
Tower body on be placed with carbon filling material layer at least provided with two grades interconvertible modularity stuffing frame (6), modularity stuffing frame on (6)
(5), spray packed tower (4) is provided with for absorbing liquid spray head (3) and demister (2)；Circulating pump (20) one end with
Degraded pond (12) connection is absorbed, the other end is connected with absorbing liquid spray head (3) by connecting tube (22).
3. organic exhaust gas multistep treatment purifier according to claim 1 and 2, is characterized in that：Described upper division board
(15) both sides are correspondingly provided with the first aeration agitation pipe (14) and the second aeration agitation pipe (16) being connected with source of oxygen (10).
4. organic exhaust gas multistep treatment purifier according to claim 3, is characterized in that：The modularity screen frame
(18) the absorption degraded pond (12) of outlet side is provided with the 3rd aeration agitation pipe (19) being connected with source of oxygen (10).
5. organic exhaust gas multistep treatment purifier according to claim 4, is characterized in that：Described source of oxygen (10) is
The mixing of any one or any two kinds of ozone, oxygen or compressed air.
6. organic exhaust gas multistep treatment purifier according to claim 5, is characterized in that：Carbon filling material layer (5) and
Charcoal Grain size controlling on charcoal filling silk screen basket (17) is between 1-5 centimetre.
7. organic exhaust gas multistep treatment purifier according to claim 6, is characterized in that：Add from powdered carbon charge door (8)
The powdered carbon for entering is controlled between 100-3000 mesh.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620974819.2U CN206008420U (en) | 2016-08-30 | 2016-08-30 | Organic exhaust gas multistep treatment purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620974819.2U CN206008420U (en) | 2016-08-30 | 2016-08-30 | Organic exhaust gas multistep treatment purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206008420U true CN206008420U (en) | 2017-03-15 |
Family
ID=58253746
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620974819.2U Expired - Fee Related CN206008420U (en) | 2016-08-30 | 2016-08-30 | Organic exhaust gas multistep treatment purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206008420U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106237804A (en) * | 2016-08-30 | 2016-12-21 | 永康市禄祥环保科技有限公司 | Organic exhaust gas multistep treatment purifier |
| CN108793382A (en) * | 2018-06-06 | 2018-11-13 | 东南大学 | A kind of filler modularized reactor of ozone catalytic |
| CN109012584A (en) * | 2018-08-07 | 2018-12-18 | 永康市禄祥环保科技有限公司 | A kind of novel absorbent charcoal and the method for handling organic exhaust gas |
-
2016
- 2016-08-30 CN CN201620974819.2U patent/CN206008420U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106237804A (en) * | 2016-08-30 | 2016-12-21 | 永康市禄祥环保科技有限公司 | Organic exhaust gas multistep treatment purifier |
| CN106237804B (en) * | 2016-08-30 | 2019-01-11 | 永康市禄祥环保科技有限公司 | Organic exhaust gas multistep treatment purification device |
| CN108793382A (en) * | 2018-06-06 | 2018-11-13 | 东南大学 | A kind of filler modularized reactor of ozone catalytic |
| CN109012584A (en) * | 2018-08-07 | 2018-12-18 | 永康市禄祥环保科技有限公司 | A kind of novel absorbent charcoal and the method for handling organic exhaust gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20170315 |