CN206762312U - A kind of organic waste gas purifying processing device - Google Patents
A kind of organic waste gas purifying processing device Download PDFInfo
- Publication number
- CN206762312U CN206762312U CN201720427781.1U CN201720427781U CN206762312U CN 206762312 U CN206762312 U CN 206762312U CN 201720427781 U CN201720427781 U CN 201720427781U CN 206762312 U CN206762312 U CN 206762312U
- Authority
- CN
- China
- Prior art keywords
- condensation chamber
- organic waste
- processing device
- body housing
- waste gas
- 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
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- 239000007789 gas Substances 0.000 title claims abstract description 42
- 239000010815 organic waste Substances 0.000 title claims abstract description 14
- 238000009833 condensation Methods 0.000 claims abstract description 34
- 230000005494 condensation Effects 0.000 claims abstract description 34
- 238000001179 sorption measurement Methods 0.000 claims abstract description 32
- 238000011084 recovery Methods 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000003892 spreading Methods 0.000 claims abstract description 14
- 238000005057 refrigeration Methods 0.000 claims abstract description 5
- 239000003463 adsorbent Substances 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 claims description 6
- 238000010521 absorption reaction Methods 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 4
- 239000011490 mineral wool Substances 0.000 claims description 3
- 238000004321 preservation Methods 0.000 claims description 3
- 239000002904 solvent Substances 0.000 claims description 3
- 239000002912 waste gas Substances 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 2
- 239000012855 volatile organic compound Substances 0.000 description 13
- 239000003960 organic solvent Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- IHICGCFKGWYHSF-UHFFFAOYSA-N C1=CC=CC=C1.CC1=CC=CC=C1.CC1=CC=CC=C1C Chemical compound C1=CC=CC=C1.CC1=CC=CC=C1.CC1=CC=CC=C1C IHICGCFKGWYHSF-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of organic waste gas purifying processing device, including body housing, adsorption box and reclaiming cover, the mutually closed condensation chamber in left and right is divided into by dividing plate inside the body housing, coil pipe is fixed with inside the condensation chamber, the coil pipe forms circulation loop by condensate liquid delivery pipe and refrigeration machine, the top of the condensation chamber is fixedly connected on air-spreading disk by blast pipe respectively, the side of the adsorption box is connected with reclaiming cover, the top of the reclaiming cover is connected to body housing by recovery tube, and the bottom of the condensation chamber is provided with atmospheric valve.The utility model carries out liquefaction recovery by the coil pipe for having condensate liquid that circulates to organic exhaust gas, the organic gas to gasify again can be caught by negative-pressure air fan, and it is delivered to by recovery tube in another condensation chamber and carries out condensation liquefaction again, improve the condensation organic efficiency of organic gas, and gas improves organic waste-gas purification efficiency eventually through being discharged after adsorption plate from exhaust outlet.
Description
Technical field
The utility model belongs to environmental protecting device technical field, and in particular to a kind of organic waste gas purifying processing device.
Background technology
VOCs treatment refers to the place that caused organic exhaust gas is adsorbed, filtered, purified in industrial processes
Science and engineering is made.Usual VOCs treatment has benzene homologues VOCs treatment, third such as formaldehyde VOCs treatment, benzene toluene dimethylbenzene
Ketone butanone VOCs treatment, ethyl acetate exhaust-gas treatment, mist of oil VOCs treatment, furfural VOCs treatment, styrene,
Acrylic acid VOCs treatment, resin VOCs treatment, additive VOCs treatment, coating cloud VOCs treatment, day that
The purification of air processing of the organic matters such as the carbon containing hydrogen-oxygen such as water VOCs treatment.
Existing VOCs treatment mode generally can not carry out liquefaction recovery to organic gas, the wasting of resources be caused, if having
Environment can also be polluted when machine exhaust-gas treatment is incomplete.
Utility model content
The purpose of this utility model is to provide a kind of organic waste gas purifying processing device, to solve in above-mentioned background technology
The problem of proposition.
To achieve the above object, the utility model provides following technical scheme:A kind of organic waste gas purifying processing device, bag
Include body housing, adsorption box and reclaiming cover, the mutually closed condensation chamber in left and right be divided into by dividing plate inside the body housing,
Coil pipe is fixed with inside the condensation chamber, the coil pipe forms circulation loop by condensate liquid delivery pipe and refrigeration machine, described cold
The top of solidifying room is fixedly connected on air-spreading disk by blast pipe respectively, and the air-spreading disk is arranged on the bottom of adsorption box, the suction
The top of attached case is provided with exhaust outlet, and the side of the adsorption box is connected with reclaiming cover, passes through recovery at the top of the reclaiming cover
Pipe is connected to body housing, and negative-pressure air fan is provided with the recovery tube, and the bottom of the condensation chamber is provided with atmospheric valve.
Preferably, the closure cavity inner bottom part that the adsorption box is formed with reclaiming cover is provided with adsorbent layer, the adsorbent
Layer is made up of carbon tetrachloride adsorption solvent.
Preferably, fixed block is fixed with the housing both sides inwall of the adsorption box, absorption is connected with the fixed block
Plate, and adsorption plate is made up of activated carbon.
Preferably, the air-spreading disk is divided into two parts, is each partly provided with the interface connected with blast pipe, and gas distribution
The surface of disk is evenly distributed with stomata,
Preferably, one layer of heat preservation layer is provided with outside the body housing, the heat-insulation layer is made up of rock wool, the body
The bottom of shell is additionally provided with the observation window for observing liquid level.
Preferably, the bottom side of one of condensation chamber is provided with exhaust gas inlet, the bottom side of another condensation chamber with
Recovery tube is fixedly connected.
Technique effect of the present utility model and advantage:The organic waste gas purifying processing device, organic exhaust gas is from exhaust gas inlet
It is interior to enter in condensation chamber, when organic gas runs into circulation and has the coil pipe of condensate liquid, become liquid from gaseous state, be collected at condensation
The bottom of room, liquid can be discharged by atmospheric valve, reclaimed, it is impossible to which timely liquefied gas enters suction by blast pipe
When in the adsorbent layer in attached case, carry out second by organic solvent and absorb, the waste gas after absorption passes through the suction in adsorption box
Discharge from exhaust outlet after attached plate, when organic gas molecule is diffused in reclaiming cover in organic solvent layer to low concentration region, lead to
The organic gas to gasify again can be caught by crossing negative-pressure air fan, and is delivered to by recovery tube in another condensation chamber again
Condensation liquefaction is carried out, improves the condensation organic efficiency of organic gas.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is mplifying structure schematic diagram at A in Fig. 1 of the present utility model;
Fig. 3 is air-spreading disk structural representation of the present utility model.
In figure:1 refrigeration machine, 2 condensate liquid delivery pipes, 3 body housings, 4 coil pipes, 5 dividing plates, 6 blast pipes, 7 condensation chambers, 8 rows
Gas port, 9 adsorption boxes, 10 adsorption plates, 11 reclaiming covers, 12 negative-pressure air fans, 13 air-spreading disks, 131 interfaces, 132 stomatas, 14 recovery tubes,
15 exhaust gas inlets, 16 atmospheric valves, 17 fixed blocks, 18 heat-insulation layers, 19 adsorbent layers.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
The utility model provides a kind of organic waste gas purifying processing device as Figure 1-3, including body housing 3,
Adsorption box 9 and reclaiming cover 11, the mutually closed condensation chamber 7 in left and right is divided into by dividing plate 5 inside the body housing 3, it is described
Coil pipe 4 is fixed with inside condensation chamber 7, the coil pipe 4 forms circulation loop by condensate liquid delivery pipe 2 and refrigeration machine 1, described cold
The top of solidifying room 7 is fixedly connected on air-spreading disk 13 by blast pipe 6 respectively, and the air-spreading disk 13 is arranged on the bottom of adsorption box 9,
The top of the adsorption box 9 is provided with exhaust outlet 8, and the side of the adsorption box 9 is connected with reclaiming cover 11, the reclaiming cover 11
Top is connected to body housing 3 by recovery tube 14, and negative-pressure air fan 12 is provided with the recovery tube 14, the condensation chamber 7
Bottom is provided with atmospheric valve 16.
Further, the closure cavity inner bottom part that the adsorption box 9 is formed with reclaiming cover 11 is provided with adsorbent layer 19, described
Adsorbent layer 19 is made up of carbon tetrachloride adsorption solvent.
Further, fixed block 17 is fixed with the housing both sides inwall of the adsorption box 9, is connected on the fixed block 17
There is adsorption plate 10, and adsorption plate 10 is made up of activated carbon.
Further, the air-spreading disk 13 divides for two parts, is each partly provided with the interface connected with blast pipe 6
131, and the surface of air-spreading disk 13 is evenly distributed with stomata 132,
Further, one layer of heat preservation layer 18 is provided with outside the body housing 3, the heat-insulation layer 18 is made up of rock wool,
The bottom of the body housing 3 is additionally provided with the observation window for observing liquid level.
Further, the bottom side of one of condensation chamber 7 is provided with exhaust gas inlet 15, the bottom of another condensation chamber 7
Side is fixedly connected with recovery tube 14.
Specifically, in use, organic exhaust gas enters in a condensation chamber 7 out of exhaust gas inlet 15, organic gas runs into stream
When being connected with the coil pipe 4 of condensate liquid, become liquid from gaseous state, be collected at the bottom of condensation chamber 7, can be with discharge liquor by atmospheric valve 16
Body, reclaimed, it is impossible to when timely liquefied gas is entered in the adsorbent layer 19 in adsorption box 9 by blast pipe 6, pass through
Organic solvent carries out second and absorbed, the waste gas after absorption by being discharged after the adsorption plate 10 in adsorption box 9 from exhaust outlet 8, when
When organic gas molecule is diffused in reclaiming cover 11 in organic solvent layer 19 to low concentration region, it can be caught by negative-pressure air fan 12
The organic gas to gasify again is caught, and is delivered to by recovery tube 14 in another condensation chamber 7 and carries out condensation liquefaction again,
Improve the condensation organic efficiency of organic gas.
Finally it should be noted that:Preferred embodiment of the present utility model is the foregoing is only, is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it can still modify to the technical scheme described in foregoing embodiments, or to which part technical characteristic
Progress equivalent substitution, all within the spirit and principles of the utility model, any modification, equivalent substitution and improvements made etc.,
It should be included within the scope of protection of the utility model.
Claims (6)
1. a kind of organic waste gas purifying processing device, including body housing (3), adsorption box (9) and reclaiming cover (11), its feature exist
In:The body housing (3) is internal to be divided into the mutually closed condensation chamber (7) in left and right, the condensation chamber (7) by dividing plate (5)
Inside is fixed with coil pipe (4), and the coil pipe (4) forms circulation loop by condensate liquid delivery pipe (2) and refrigeration machine (1), described
The top of condensation chamber (7) is fixedly connected on air-spreading disk (13) by blast pipe (6) respectively, and the air-spreading disk (13) is arranged on absorption
The bottom of case (9), the top of the adsorption box (9) are provided with exhaust outlet (8), side and the reclaiming cover (11) of the adsorption box (9)
It is connected, the top of the reclaiming cover (11) is connected to body housing (3) by recovery tube (14), pacifies on the recovery tube (14)
Equipped with negative-pressure air fan (12), the bottom of the condensation chamber (7) is provided with atmospheric valve (16).
A kind of 2. organic waste gas purifying processing device according to claim 1, it is characterised in that:The adsorption box (9) with
The closure cavity inner bottom part that reclaiming cover (11) is formed is provided with adsorbent layer (19), and the adsorbent layer (19) is adsorbed by carbon tetrachloride
Solvent forms.
A kind of 3. organic waste gas purifying processing device according to claim 1, it is characterised in that:The adsorption box (9)
Fixed block (17) is fixed with the inwall of housing both sides, adsorption plate (10), and adsorption plate (10) are connected with the fixed block (17)
It is made up of activated carbon.
A kind of 4. organic waste gas purifying processing device according to claim 1, it is characterised in that:The air-spreading disk (13) point
For two parts, the interface (131) with blast pipe (6) connection is each partly provided with, and the surface of air-spreading disk (13) is uniformly divided
It is furnished with stomata (132).
A kind of 5. organic waste gas purifying processing device according to claim 1, it is characterised in that:The body housing (3)
Outside is provided with one layer of heat preservation layer (18), and the heat-insulation layer (18) is made up of rock wool, and the bottom of the body housing (3) is also set up
There is the observation window for observing liquid level.
A kind of 6. organic waste gas purifying processing device according to claim 1, it is characterised in that:One of condensation chamber
(7) bottom side is provided with exhaust gas inlet (15), and the bottom side of another condensation chamber (7) is fixedly connected with recovery tube (14).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720427781.1U CN206762312U (en) | 2017-04-22 | 2017-04-22 | A kind of organic waste gas purifying processing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201720427781.1U CN206762312U (en) | 2017-04-22 | 2017-04-22 | A kind of organic waste gas purifying processing device |
Publications (1)
Publication Number | Publication Date |
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CN206762312U true CN206762312U (en) | 2017-12-19 |
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CN201720427781.1U Expired - Fee Related CN206762312U (en) | 2017-04-22 | 2017-04-22 | A kind of organic waste gas purifying processing device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110215799A (en) * | 2018-11-28 | 2019-09-10 | 朴骏培 | Oil vapour recyclable device |
CN111482040A (en) * | 2019-01-29 | 2020-08-04 | 内蒙古环保投资集团有限公司 | Cryogenic micro-negative pressure circulating purification device and VOCs treatment method based on same |
CN112473318A (en) * | 2020-11-29 | 2021-03-12 | 云南能投化工有限责任公司 | Production of acetylene gas is retrieved with degasification tower that is difficult for blockking up to carbide slag thick liquid |
-
2017
- 2017-04-22 CN CN201720427781.1U patent/CN206762312U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110215799A (en) * | 2018-11-28 | 2019-09-10 | 朴骏培 | Oil vapour recyclable device |
CN111482040A (en) * | 2019-01-29 | 2020-08-04 | 内蒙古环保投资集团有限公司 | Cryogenic micro-negative pressure circulating purification device and VOCs treatment method based on same |
CN112473318A (en) * | 2020-11-29 | 2021-03-12 | 云南能投化工有限责任公司 | Production of acetylene gas is retrieved with degasification tower that is difficult for blockking up to carbide slag thick liquid |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
EE01 | Entry into force of recordation of patent licensing contract | ||
EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Yunnan yanyuxuan Environmental Engineering Co.,Ltd. Assignor: YUNNAN WATER ENVIRONMENTAL ENGINEERING CO.,LTD. Contract record no.: X2023530000005 Denomination of utility model: An organic waste gas purification and treatment device Granted publication date: 20171219 License type: Common License Record date: 20230306 |
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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: 20171219 |