CN203635019U - Spray paint waste gas treatment device - Google Patents
Spray paint waste gas treatment device Download PDFInfo
- Publication number
- CN203635019U CN203635019U CN201420016413.4U CN201420016413U CN203635019U CN 203635019 U CN203635019 U CN 203635019U CN 201420016413 U CN201420016413 U CN 201420016413U CN 203635019 U CN203635019 U CN 203635019U
- Authority
- CN
- China
- Prior art keywords
- waste gas
- demister
- corona discharge
- plasma
- low temp
- 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
- 239000002912 waste gas Substances 0.000 title claims abstract description 76
- 239000007921 spray Substances 0.000 title claims abstract description 35
- 239000003973 paint Substances 0.000 title abstract description 18
- 238000005507 spraying Methods 0.000 claims abstract description 35
- 210000002381 Plasma Anatomy 0.000 claims abstract description 34
- 238000004140 cleaning Methods 0.000 claims abstract description 32
- 239000007789 gas Substances 0.000 claims abstract description 28
- 238000005406 washing Methods 0.000 claims abstract description 18
- 238000007599 discharging Methods 0.000 claims abstract description 7
- 239000004922 lacquer Substances 0.000 claims description 27
- 239000011248 coating agent Substances 0.000 claims description 11
- 238000000576 coating method Methods 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 9
- 241000628997 Flos Species 0.000 claims description 5
- 239000006260 foam Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 abstract description 7
- 238000001035 drying Methods 0.000 abstract description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N o-xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 abstract description 4
- 238000003915 air pollution Methods 0.000 abstract 1
- 239000002957 persistent organic pollutant Substances 0.000 abstract 1
- 239000003595 mist Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 7
- 230000002378 acidificating Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000011068 load Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Abstract
The utility model relates to a spray paint waste gas treatment device which is used for treating waste gas discharged from a spray paint waste gas discharging port. The spray paint waste gas treatment device comprises a wet-type cyclone separator, a corona discharging low-temperature plasma waste gas purifying device and a spraying washing tower, which are sequentially connected with the spray paint waste gas discharging port, wherein a gas outlet of the wet-type cyclone separator is connected with a gas inlet of the corona discharging low-temperature plasma waste gas purifying device, a gas outlet of the corona discharging low-temperature plasma waste gas purifying device is connected with a gas inlet of the spraying washing tower, and the spraying washing tower is provided with an exhaust port which is communicated with the atmosphere. The spray paint waste gas treatment device is designed for purifying the spray paint waste gas, the air pollution caused by the volatilization of organic pollutants such as methylbenzene and dimethylbenzene in the paint spraying and drying process can be reduced at relatively low cost, and a purpose of clean emission can be realized.
Description
Technical field
The utility model relates to waste gas purification processing technology field, relates in particular to a kind of lacquer spraying waste gas treating apparatus.
Background technology
Spraying paint is a kind of very common process of surface treatment, and in now widely used paint, the organic solvents such as benzene,toluene,xylene, NMHC occupy very large ratio.Spray paint and dry process in, these organic solvents can evaporate in air, form the pollution to air.Existing paint-spraying production line is all provided with air exhausting device at paint spray booth and baking room, and the organic matter volatilizing in paint is discharged.The emission-control equipment that at present only had a small amount of paint-spraying production line design and installation, in these emission-control equipments, majority is to adopt sorbing material to process organic pollution.The sorbing materials such as active carbon are to utilize the micro-pore of material surface that the molecule particle of pollutant is fixed, and in lacquer spraying waste gas, contain the dry coating cloud of significant proportion, these coating clouds are attached to sorbing material surface, after dry, the micropore of sorbing material can be blocked, stop sorbing material further to adsorb, because paint is dry rear firmly abnormal, sorbing material cannot be regenerated simultaneously, must change.Therefore adopt absorption method to process lacquer spraying waste gas and there is very large difficulty.Because the tolerance of lacquer spraying waste gas is huge, some efficient processing methods are as combustion method needs a large amount of heat energy, are that the producer of spraying paint often cannot bear.
Chinese patent (N202654901U) discloses a kind of absorbent charcoal adsorber of paint spray booth, adsorbs with two-layer active carbon, and this mode gas does not pass through pre-filtering, and the utilization rate of active carbon is reduced, and replacement frequency increases, and cost is huge.Therefore need to develop the treating apparatus of a kind of anti-pollution, low operating cost.
Utility model content
The technical problems to be solved in the utility model is: overcome the expensive technical problem of lacquer spraying waste gas treating apparatus in prior art, a kind of lacquer spraying waste gas treating apparatus is provided, under lower cost, reduce spray paint and dry process in the pollution that causes in evaporateing into air of the organic pollution such as toluene, dimethylbenzene.
The utility model solves the technical scheme that its technical problem adopts: a kind of lacquer spraying waste gas treating apparatus, the waste gas of discharging for the treatment of lacquer spraying waste gas floss hole, described lacquer spraying waste gas treating apparatus comprises the wet cyclone being connected successively with lacquer spraying waste gas floss hole, corona discharge low temp cleaning plant for waste gas of plasma and spray washing tower, described wet cyclone gas outlet connects the air inlet of corona discharge low temp cleaning plant for waste gas of plasma, the gas outlet of described corona discharge low temp cleaning plant for waste gas of plasma connects the air inlet of described spray washing tower, described spray washing tower is provided with the exhaust outlet communicating with atmosphere.
Further, described Waste gas outlet is communicated with the air inlet of the bottom that is positioned at described wet cyclone by pipeline, and the bottom of wet cyclone has liquid and/or solid-state coating cloud is concentrated outlet.
Further, described lacquer spraying waste gas treating apparatus also comprises demister, described demister is located between wet cyclone and corona discharge low temp cleaning plant for waste gas of plasma, the gas outlet of described wet cyclone is connected with the air inlet of described demister, and the gas outlet of described demister is connected with the air inlet of corona discharge low temp cleaning plant for waste gas of plasma.
Further, described demister is baffle plate type demister, the air foam separator that described baffle plate type demister is made up of several deflection plates, and described baffle plate type demister is two groups.
Further, described baffle plate type demister is made up of stainless steel.
Further, described corona discharge low temp cleaning plant for waste gas of plasma comprises housing and is located at the corona discharge low temp plasma electrode in housing.
Further, in described housing, be provided with the cleaning device that can clean described corona discharge low temp plasma electrode.
Further, described spray washing tower has two groups of spray heads.
The beneficial effects of the utility model are, lacquer spraying waste gas treating apparatus of the present utility model is removed the liquid and/or solid-state coating cloud that has a strong impact on described lacquer spraying waste gas treating apparatus operation in waste gas by wet cyclone, can further remove mist by flowing board-like demister, then remove the organic pollution in waste gas by corona discharge low temp cleaning plant for waste gas of plasma, remove by spray washing tower the acidic oxide forming after organic pollution oxidation again, emit by exhaust outlet through the waste gas of processing.The utility model under lower cost, reduce spray paint and dry process in the pollution that causes in evaporateing into air of the organic pollution such as toluene, dimethylbenzene, reached the object of clean emission.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is the structural representation of a kind of embodiment of the utility model.
In figure: 1, Waste gas outlet; 2, wet cyclone; 3, demister; 4, corona discharge low temp plasma electrode; 5, cleaning device; 6, discharge low-temperature cleaning plant for waste gas of plasma; 7, outlet; 8, spray washing tower; 9, spray head; 10, exhaust outlet.
The specific embodiment
By reference to the accompanying drawings the utility model is described in further detail now.These accompanying drawings are the schematic diagram of simplification, and basic structure of the present utility model is only described in a schematic way, and therefore it only shows the formation relevant with the utility model.
As shown in Figure 1, described lacquer spraying waste gas treating apparatus of the present utility model comprises the wet cyclone 2, corona discharge low temp cleaning plant for waste gas of plasma 6 and the spray washing tower 8 that are connected successively with lacquer spraying waste gas floss hole 1, described wet cyclone 2 gas outlets connect the air inlet of corona discharge low temp cleaning plant for waste gas of plasma 6, the gas outlet of described corona discharge low temp cleaning plant for waste gas of plasma 6 connects the air inlet of described spray washing tower 8, and described spray washing tower 8 is provided with the exhaust outlet 10 communicating with atmosphere.
The waste gas that enters described wet cyclone 2 through floss hole 1 is subject to revolving wind action and produces strong rotation, liquid and solid-state coating cloud is thrown toward the wall of wet cyclone 2 under the action of the centrifugal, under Action of Gravity Field, liquid and solid-state coating cloud falls through concentrating outlet 7 to discharge along wall.Gas after separation enters corona discharge low temp cleaning plant for waste gas of plasma 6 from the gas outlet of wet cyclone 2.
For the liquid state to larger in waste gas and solid-state coating cloud carry out pre-separation, to alleviate the load of wet cyclone 2, preferably, described Waste gas outlet 1 is communicated with the air inlet of the bottom that is positioned at described wet cyclone 2 by pipeline, and the bottom of wet cyclone 2 has liquid and/or solid-state coating cloud is concentrated outlet 7.Because from bottom air inlet, can make full use of the lower space of wet cyclone 2.
Entrainment in the gas of processing through wet cyclone 2, and these mist diameters are very little, described mist need to be removed, therefore, described lacquer spraying waste gas treating apparatus also comprises demister 3, described demister 3 is located between wet cyclone 2 and corona discharge low temp cleaning plant for waste gas of plasma 6, the gas outlet of described wet cyclone 2 is connected with the air inlet of described demister 3, and the gas outlet of described demister 3 is connected with the air inlet of corona discharge low temp cleaning plant for waste gas of plasma 6.
In order further to improve the efficiency of demist, described demister 3 is baffle plate type demister, the air foam separator that described baffle plate type demister is made up of several deflection plates, and described baffle plate type demister is two groups.When the waste gas that contains mist is flowed through baffle plate type demister with certain speed, in baffle plate type demister, the bend of V-type deflection plate composition causes the sharply variation of fluid flow direction, make to have compared with the mist of large inertia and deflection plate and collide and be attached on deflection plate surface, mist is separated from mobile gas.And gas is unimpeded due to the runner spaciousness forming between deflection plate, thereby can smooth and easy passing through.Two groups of baffle plate type demisters have increased the chance that mist is captured, and the mist not being removed is captured through identical effect at next group baffle plate type demister, thereby has greatly improved demist efficiency.Gas, by after baffle plate type demister, does not basically contain mist.
In order to strengthen the corrosion resistance of described baffle plate type demister, preferentially, described baffle plate type demister is made up of stainless steel.
Described corona discharge low temp cleaning plant for waste gas of plasma 6 comprises housing and is located at the corona discharge low temp plasma electrode 4 in housing.
Contaminated and cannot process waste gas due to corona discharge low temp plasma electrode 4 for fear of emission-control equipment, preferably, in described housing, be provided with the cleaning device 5 that can clean described corona discharge low temp plasma electrode 4.
In order to remove the acidic oxide forming after oxidation operation, preferably, described spray washing tower 8 comprises two groups of spray heads 9, and described spray head 9 sprays alkaline water, the waste gas of processing is washed, and after the acidic oxide forming after removal oxidation operation, gas is discharged from exhaust outlet 10.
The operation principle of lacquer spraying waste gas treating apparatus of the present utility model is as follows: first by wet cyclone 2, the liquid state and the solid-state coating cloud that in waste gas, have a strong impact on treating apparatus operation are removed, liquid and solid-state coating cloud is through concentrating outlet 7 to discharge; Gas is further removed mist by the board-like demister 3 of stream again; Then utilize resistant to pollution corona discharge low temp plasma electrode 4 in discharge low-temperature cleaning plant for waste gas of plasma 6 that the organic pollution being dissolved in gas is decomposed to removal; Finally utilize the spray head 9 in spray washing tower 8 to spray alkaline water, the gas of processing is washed, after the acidic oxide forming after removal oxidation operation, gas is discharged through exhaust outlet 10, reaches the object of clean emission.
Take above-mentioned foundation desirable embodiment of the present utility model as enlightenment, by above-mentioned description, relevant staff can, not departing from the scope of this utility model technological thought, carry out various change and modification completely.The technical scope of this utility model is not limited to the content on description, must determine its technical scope according to claim scope.
Claims (8)
1. a lacquer spraying waste gas treating apparatus, the waste gas of discharging for the treatment of lacquer spraying waste gas floss hole (1), it is characterized in that, comprise the wet cyclone (2) connecting successively, corona discharge low temp cleaning plant for waste gas of plasma (6) and spray washing tower (8), described wet cyclone (2) gas outlet connects the air inlet of corona discharge low temp cleaning plant for waste gas of plasma (6), the gas outlet of described corona discharge low temp cleaning plant for waste gas of plasma (6) connects the air inlet of described spray washing tower (8), described spray washing tower (8) is provided with the exhaust outlet (10) communicating with atmosphere.
2. lacquer spraying waste gas treating apparatus as claimed in claim 1, it is characterized in that, described Waste gas outlet (1) is communicated with the air inlet of the bottom that is positioned at described wet cyclone (2) by pipeline, and the bottom of wet cyclone (2) has liquid and/or solid-state coating cloud is concentrated outlet (7).
3. lacquer spraying waste gas treating apparatus as claimed in claim 1, it is characterized in that, also comprise demister (3), described demister is located between wet cyclone (2) and corona discharge low temp cleaning plant for waste gas of plasma (6), the gas outlet of described wet cyclone (2) is connected with the air inlet of described demister (3), and the gas outlet of described demister (3) is connected with the air inlet of corona discharge low temp cleaning plant for waste gas of plasma (6).
4. lacquer spraying waste gas treating apparatus as claimed in claim 3, it is characterized in that, described demister (3) is baffle plate type demister, the air foam separator that described baffle plate type demister is made up of several V-type deflection plates, and described baffle plate type demister is two groups.
5. lacquer spraying waste gas treating apparatus as claimed in claim 4, is characterized in that, described baffle plate type demister is made up of stainless steel.
6. lacquer spraying waste gas treating apparatus as claimed in claim 1, is characterized in that, described corona discharge low temp cleaning plant for waste gas of plasma (6) comprises housing and is located at the corona discharge low temp plasma electrode (4) in housing.
7. lacquer spraying waste gas treating apparatus as claimed in claim 6, is characterized in that, is provided with the cleaning device (5) that can clean described corona discharge low temp plasma electrode (4) in described housing.
8. lacquer spraying waste gas treating apparatus as claimed in claim 1, is characterized in that, has two groups of spray heads (9) in described spray washing tower (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420016413.4U CN203635019U (en) | 2014-01-13 | 2014-01-13 | Spray paint waste gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420016413.4U CN203635019U (en) | 2014-01-13 | 2014-01-13 | Spray paint waste gas treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203635019U true CN203635019U (en) | 2014-06-11 |
Family
ID=50866303
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420016413.4U Expired - Fee Related CN203635019U (en) | 2014-01-13 | 2014-01-13 | Spray paint waste gas treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203635019U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103736351A (en) * | 2014-01-13 | 2014-04-23 | 苏州克利亚环保科技有限公司 | Painting-waste-gas treating device |
| CN104083978A (en) * | 2014-07-07 | 2014-10-08 | 中国轻工业武汉设计工程有限责任公司 | Exhausting-recycling device of green liquid dissolving tank |
| CN104906910A (en) * | 2015-06-24 | 2015-09-16 | 上海大众汽车有限公司 | Paint mist purifying device |
| CN109876649A (en) * | 2017-12-06 | 2019-06-14 | 天长市金陵电子有限责任公司 | A kind of painting workshop emission-control equipment |
-
2014
- 2014-01-13 CN CN201420016413.4U patent/CN203635019U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103736351A (en) * | 2014-01-13 | 2014-04-23 | 苏州克利亚环保科技有限公司 | Painting-waste-gas treating device |
| CN104083978A (en) * | 2014-07-07 | 2014-10-08 | 中国轻工业武汉设计工程有限责任公司 | Exhausting-recycling device of green liquid dissolving tank |
| CN104083978B (en) * | 2014-07-07 | 2015-11-18 | 中国轻工业武汉设计工程有限责任公司 | A kind of green liquor dissolving tank exhaust recovery device |
| CN104906910A (en) * | 2015-06-24 | 2015-09-16 | 上海大众汽车有限公司 | Paint mist purifying device |
| CN104906910B (en) * | 2015-06-24 | 2016-08-31 | 上汽大众汽车有限公司 | Paint mist purification treatment device |
| CN109876649A (en) * | 2017-12-06 | 2019-06-14 | 天长市金陵电子有限责任公司 | A kind of painting workshop emission-control equipment |
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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: 20140611 Termination date: 20180113 |