CN209060853U - Spraying industry organic volatile recyclable device - Google Patents
Spraying industry organic volatile recyclable device Download PDFInfo
- Publication number
- CN209060853U CN209060853U CN201821783450.2U CN201821783450U CN209060853U CN 209060853 U CN209060853 U CN 209060853U CN 201821783450 U CN201821783450 U CN 201821783450U CN 209060853 U CN209060853 U CN 209060853U
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- China
- Prior art keywords
- gas
- organic volatile
- storehouse
- exhaust
- absorption
- 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
- 238000005507 spraying Methods 0.000 title claims abstract description 27
- 238000010521 absorption reaction Methods 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 238000003860 storage Methods 0.000 claims abstract description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000000926 separation method Methods 0.000 claims abstract description 16
- 239000007921 spray Substances 0.000 claims abstract description 14
- 230000007306 turnover Effects 0.000 claims abstract description 10
- 239000002131 composite material Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000003921 oil Substances 0.000 claims description 22
- 239000002699 waste material Substances 0.000 claims description 11
- 239000010687 lubricating oil Substances 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 238000005086 pumping Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 9
- 239000003973 paint Substances 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 6
- 239000011248 coating agent Substances 0.000 abstract description 5
- 238000000576 coating method Methods 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 2
- 239000011162 core material Substances 0.000 description 6
- 238000001914 filtration Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000006096 absorbing agent Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000012855 volatile organic compound Substances 0.000 description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 235000013162 Cocos nucifera Nutrition 0.000 description 1
- 244000060011 Cocos nucifera Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000010761 intermediate fuel oil Substances 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of spraying industry organic volatile recyclable devices, spray-absorption tank with spraying exhaust inlet pipe and appendix, oil storage pool is arranged in bottom, positioned at the top of oil storage pool, umbellate form atomizer and turnover plate type liquid-blocking unit are set, the inlet tube of oil transfer pump is connected to oil storage pool, its outlet is connected to atomizer, the appendix of spray-absorption tank top setting is connected to the air inlet of gas-liquid separation device by the first air-introduced machine, and appendix is deep into the water in gas-liquid separation device aqueous absorption storehouse, the exhaust pipe in gas-liquid separation device gas storage storehouse is connected to the air inlet of composite activated carbon absorption plant, the exhaust pipe of exhaust outlet connection is discharged by the second air-introduced machine.The utility model process structure is reasonable, and low energy consumption, sprays that draw scattered exhaust gas absorption, the ability of purification strong to the paint of collection, coating, and making that treated, spraying industry organic volatile exhaust gas accomplishes qualified discharge.
Description
Technical field
The utility model belongs to spraying industry organic volatile recyclable device, especially a kind of spraying industry organic volatile
Recyclable device.
Background technique
Volatile organic matter refers to boiling temperature at 35-180 °C, and saturated vapour pressure is more than a system of 133.32 pas at room temperature
Column organic compound is mainly derived from petroleum, chemical industry, rubber, building materials, the industries such as paint.The paint that spraying industry uses, coating
In contain suitable component " polarity, nonpolarity " organic solvent, such as: toluene, dimethylbenzene, ethyl acetate etc..Such solvent is not
The solidification of lacquer painting is participated in, but is bled around with being spilt into air in construction, solidification process, spraying exhaust gas is formed, this is useless
Contain a large amount of volatile organic matter (VOCs) in gas.Volatile organic matter (VOCs) recovery processing technology mainly has at present: inhaling
Attached absorption techniques, condensation technology, film recovery technology, PhotoelectrochemicalTechnique Technique etc..Such as: patent 201720835114.8,
201110068055.2,20140317870.4, though the above technology has certain practicability, in the presence of the device is complicated, body
The defects of product is big, and energy consumption is high, investment is big is not suitable for dissipating, small, micro- auto repair, small device manufacture Deng little Wei enterprise.
Utility model content
The purpose of this utility model is to provide a kind of spraying industry organic volatile recyclable device, process structure is closed
Reason, low energy consumption, sprays that draw scattered exhaust gas absorption, the ability of purification strong to the paint of collection, coating, the spraying industry that makes that treated
Organic volatile exhaust gas accomplishes qualified discharge.
Purpose of the utility model is realized as follows: a kind of spraying industry organic volatile recyclable device, has spraying
The spray-absorption tank of exhaust inlet pipe and appendix, the oil storage pool equipped with waste lubricating oil is arranged in bottom, positioned at oil storage pool
Umbellate form atomizer and turnover plate type liquid-blocking unit is arranged in top, and the inlet tube of oil transfer pump is connected to oil storage pool, and outlet connects
Then the appendix of atomizer, the setting of spray-absorption tank top is connected to the air inlet of gas-liquid separation device by the first air-introduced machine
Mouthful, and appendix is deep into the water in gas-liquid separation device aqueous absorption storehouse, and the exhaust pipe in gas-liquid separation device gas storage storehouse connects
Then the exhaust pipe of the air inlet of composite activated carbon absorption plant, exhaust outlet connection is discharged by the second air-introduced machine.
Traditional aqueous spray desorption is changed to according to " similar compatibility " principle with waste lubricating oil liquid by the utility model
Liquid is adsorbed as spray, the suction to paint, the aerial organic solvent of coating disperse in spraying process greatly improved
Attached ability, the utility model are divided into organic volatile oiliness (nonpolarity) spray-absorption section, gas-liquid separation section, and composite activated carbon is inhaled
Receive section.Oiliness spray-absorption Duan Weiyi pyramidal structure, bottom be it is tapered, be convenient for blowdown.Internal structure is respectively oil from bottom to top
Liquid storage pool, three-level sieve (10 millimeters of aperture) umbellate form atomizer, secondary panel turnover formula liquid-blocking unit.Aqueous absorber portion is divided into one
The aqueous container of Intermediate Gray partition.Composite activated carbon absorber portion is a rectangle multistage closed structure, and two-stage axial flow blower is device
The power source of exhaust gas movement.
Gas moves from bottom to top in tower, and waste lubricating oil liquid oil absorbing liquid is by the umbellate form in circulating pump input absorption tower
Atomizer, from top to bottom radial injection, exhaust gas are inversely contacted with absorbing liquid, and similar compatibility is largely absorbed.
Oil liquid is used after the filtering of 200 mesh with 5W30 or less (preferably 0W20) waste and old vehicle lubricating oil, atomizing spray head
Using MP system spray head, MP15-20 spray head is specifically used, is vertically mounted on the top of netted umbellate form, selects pumping pressure big
In 0.3Mpa, flow is greater than 150L/h as oil liquid delivery pump.Also diesel fuel burner intermediate fuel oil atomizer the whole series component can be selected.
Exterior 200 mesh barrel type filter in oil pump inlet end is conveniently replaceable filter core.
Two groups of turnover plate type liquid-blocking units are similar shutter, and for unidirectional aperture less than 65 °, dress is made in two groups of directions
With the flow velocity can continuously to change air-flow, flow direction collides it on blade, compression and liquid phase substance falls naturally after agglomerating,
Realize gas-liquid separation.
Aqueous absorber portion is the aqueous container of an Intermediate Gray partition.Respectively aqueous adsorbs storehouse, does storehouse.Aqueous liquid level is lower than
The port on partition top, exhaust pipe go deep into aqueous absorption orlop portion exhaust gas under the action of blower and wash through aqueous, institute is desorbed
Containing (polarity) hydroaropic substance.
Efficiently the core material for after the desorption of volatile organic compounds being subsequent combined filtration is extended by two sections
Use the replacement cycle.Combined filtration using cocoanut active charcoal with cabinet second level mode, the spraying industry organic volatile that makes that treated
Exhaust gas accomplishes qualified discharge.
The utility model only can need to be installed on the exhaust duct of existing equipment and can be run with modularization.To collected
It sprays disperse exhaust gas and carries out level-one oil liquid spray adsorption treatment, second level gas-liquid separation, three-level aqueous adsorption treatment, the compound work of level Four
Qualified discharge after property charcoal adsorption treatment, has accomplished the treatment of wastes with processes of wastes against one another.
The utility model process structure is reasonable, and low energy consumption, draws scattered exhaust gas to the paint of collection, coating spraying and adsorbs, only
The ability of change is strong, and making that treated, spraying industry organic volatile exhaust gas accomplishes qualified discharge.
Detailed description of the invention
The utility model is further described below in conjunction with attached drawing, Fig. 1 is the signal of the utility model front view structure
Figure.
Specific embodiment
A kind of spraying industry organic volatile recyclable device, as shown in Figure 1, having spraying exhaust inlet pipe 2 and appendix 3
Spray-absorption tank 1, bottom is arranged the oil storage pool 4 equipped with waste lubricating oil, umbellate form mist is arranged positioned at the top of oil storage pool 4
Change spray head 6 and turnover plate type liquid-blocking unit 7, the inlet tube of oil transfer pump 5 are connected to oil storage pool 4, outlet is connected to atomizer
6, the appendix 3 being arranged at the top of spray-absorption tank 1 is connected to the air inlet of gas-liquid separation device 9 by the first air-introduced machine 8, and
Appendix 3 is deep into the water in 9 aqueous of gas-liquid separation device absorption storehouse, and the exhaust pipe in 9 gas storage storehouse of gas-liquid separation device is connected to
The exhaust pipe of the air inlet of composite activated carbon absorption plant 11, exhaust outlet connection is discharged by the second air-introduced machine 14.Oil storage pool 4
In waste lubricating oil be the waste and old vehicle lubricating oil of 5W30 or less or 0W20, through 200 mesh filter.Turnover plate type liquid-blocking unit 7 is second level
Turnover plate type liquid-blocking unit, structure are venetian blind type liquid-blocking unit, the inclined direction of first order venetian blind type wind deflector and the
The inclined direction of second level venetian blind type wind deflector is on the contrary, the spacing between the adjacent wind deflector of its every grade venetian blind type liquid-blocking unit is
5-10cm.The structure of gas-liquid separation device 9 is that upright diaphragm plate 10 is arranged in the bottom in closed cuboid box body, will
Rectangular box is divided into aqueous absorption storehouse and gas storage storehouse, and wherein aqueous absorption storehouse is connected to the top in gas storage storehouse, top connection
The width of port is 25-30cm, and the length of port and the width of cabinet are equal, is connected to gas transmission on the top surface in aqueous absorption storehouse
Pipe 3 is connected to exhaust pipe on the top surface in gas storage storehouse.The structure of composite activated carbon absorption plant 11 is by first order activity carbon filtration
Core 12 and second level active carbon filter core 13 are constituted, and exhaust gas first passes through the filtering of first order active carbon filter core 12, living using the second level
Property filtration core 13 filter.Atomizer 6 uses MP system spray head, and specification is MP15-20 spray head.The pumping pressure of oil transfer pump 5 is
0.3MPa, flow are greater than 150L/h.
Claims (7)
1. a kind of spraying industry organic volatile recyclable device, it is characterized in that: having spraying exhaust inlet pipe (2) and appendix
(3) oil storage pool (4) equipped with waste lubricating oil is arranged in spray-absorption tank (1), bottom, is located above oil storage pool (4) and sets
Umbellate form atomizer (6) and turnover plate type liquid-blocking unit (7) are set, the inlet tube of oil transfer pump (5) is connected to oil storage pool (4), goes out
Mouth pipe is connected to atomizer (6), and the appendix (3) being arranged at the top of spray-absorption tank (1) is connected to by the first air-introduced machine (8)
The air inlet of gas-liquid separation device (9), and appendix (3) is deep into the water in gas-liquid separation device (9) aqueous absorption storehouse, gas
The exhaust pipe in liquid separating apparatus (9) gas storage storehouse is connected to the air inlet of composite activated carbon absorption plant (11), exhaust outlet connection
Exhaust pipe pass through the second air-introduced machine (14) be discharged.
2. spraying industry organic volatile recyclable device according to claim 1, it is characterized in that: useless in oil storage pool (4)
Lubricating oil is the waste and old vehicle lubricating oil of 5W30 or less or 0W20, is filtered through 200 mesh.
3. spraying industry organic volatile recyclable device according to claim 1, it is characterized in that: turnover plate type liquid-blocking unit
It (7) is secondary panel turnover formula liquid-blocking unit, structure is venetian blind type liquid-blocking unit, the inclination of first order venetian blind type wind deflector
Direction is with the inclined direction of second level venetian blind type wind deflector on the contrary, between the adjacent wind deflector of its every grade venetian blind type liquid-blocking unit
Spacing be 5-10cm.
4. spraying industry organic volatile recyclable device according to claim 1, it is characterized in that: gas-liquid separation device (9)
Structure be that upright diaphragm plate (10) are arranged in bottom in closed cuboid box body, rectangular box is divided into water
Liquid adsorbs storehouse and gas storage storehouse, and wherein aqueous absorption storehouse is connected to the top in gas storage storehouse, and the width that top is connected to port is 25-
30cm, the length of port and the width of cabinet are equal, appendix (3) are connected on the top surface in aqueous absorption storehouse, in gas storage storehouse
Top surface on be connected to exhaust pipe.
5. spraying industry organic volatile recyclable device according to claim 1, it is characterized in that: composite activated carbon absorbs dress
The structure for setting (11) is to be made of first order active carbon filter core (12) and second level active carbon filter core (13), and exhaust gas first passes through first
Grade active carbon filter core (12) filters, and filters using second level active carbon filter core (13).
6. spraying industry organic volatile recyclable device according to claim 1, it is characterized in that: atomizer (6) uses
MP system spray head, specification are MP15-20 spray head.
7. spraying industry organic volatile recyclable device according to claim 1, it is characterized in that: the pumping of oil transfer pump (5)
Pressure is 0.3MPa, and flow is greater than 150L/h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821783450.2U CN209060853U (en) | 2018-10-31 | 2018-10-31 | Spraying industry organic volatile recyclable device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821783450.2U CN209060853U (en) | 2018-10-31 | 2018-10-31 | Spraying industry organic volatile recyclable device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209060853U true CN209060853U (en) | 2019-07-05 |
Family
ID=67097143
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821783450.2U Expired - Fee Related CN209060853U (en) | 2018-10-31 | 2018-10-31 | Spraying industry organic volatile recyclable device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209060853U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN119240556A (en) * | 2024-09-20 | 2025-01-03 | 安徽信息工程学院 | A VOCs waste gas low temperature liquefaction device |
-
2018
- 2018-10-31 CN CN201821783450.2U patent/CN209060853U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN119240556A (en) * | 2024-09-20 | 2025-01-03 | 安徽信息工程学院 | A VOCs waste gas low temperature liquefaction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20190705 Termination date: 20211031 |