CN205517197U - Organic gas recovery system - Google Patents
Organic gas recovery system Download PDFInfo
- Publication number
- CN205517197U CN205517197U CN201620111252.6U CN201620111252U CN205517197U CN 205517197 U CN205517197 U CN 205517197U CN 201620111252 U CN201620111252 U CN 201620111252U CN 205517197 U CN205517197 U CN 205517197U
- Authority
- CN
- China
- Prior art keywords
- active carbon
- pipeline
- inlet manifold
- recovery system
- connects
- 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
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model relates to an organic gas recovery system, including the whirl tower, surface cooler and the three active carbon adsorption jar of arranging side by side, the end connection activated carbon filter of surface cooler, activated carbon filter's export is fixed with the first inlet manifold who is connected with three active carbon adsorption jar, one side of first inlet manifold is equipped with second inlet manifold and house steward dry air, the top middle part of three active carbon adsorption jar all is equipped with the active carbon feed inlet, the air inlet of active carbon feed inlet one side pass through the pipeline respectively with first inlet manifold, the total union coupling of second inlet manifold and dry air, the gas outlet of active carbon feed inlet opposite side is all through pipe connection exhaust manifold, the bottom of three active carbon adsorption jar is all through the pipe connection condenser, pipe connection layering groove is passed through to the bottom of condenser, the one side in layering groove is passed through the pipe connection and is retrieved the jar. The utility model discloses an organic gas recovery system novel structure, organic solvent's cost recovery is low, stable performance, long service life.
Description
Technical field
This utility model relates to a kind of organic gas recovery system.
Background technology
At present at dyestuff, medicine, coating, plastics, sensitive material, synthetic rubber, chemistry fibre
All can produce big during the production and application of dimension and many petrochemicals and coke chemicals
The organic exhaust gas of amount.Its concentration is mostly at 1000-3000mg/m3Left and right, these organic exhaust gas
Directly emptying not only environment is caused severe contamination, be detrimental to health and ecological environment, and
And also can cause the waste of a large amount of precious resources.And the purified treatment that China is to industrial organic exhaust gas
Technology mainly uses absorption method, and adsorbing material is mainly activated carbon.But these devices exist
Common issue is that equipment is relative complex, fault rate is higher, floor space is bigger；One-time investment
Relatively big, it is not suitable for medium-sized and small enterprises, is unfavorable for marketing.Simultaneously because the reason on She Ji,
Oil-water separation is thorough not, easily causes secondary pollution.Therefore it is badly in need of a kind of organic gas to reclaim
System.
Utility model content
For solving above-mentioned technical problem, this utility model provides a kind of organic gas recovery system.
Organic gas recovery system of the present utility model, including eddy flow tower, surface cooler and three also
The absorbent charcoal adsorption tank that arrangement is put, connecting fan between described eddy flow tower and surface cooler, surface cooler
End connect active carbon filter, the outlet of active carbon filter is fixed with and three activated carbons
Adsorbing tank connected first inlet manifold, the side of the first inlet manifold is provided with the second inlet manifold
With dry air house steward, the top middle portion of three absorbent charcoal adsorption tanks is equipped with active carbon material feeding
Mouthful, the air inlet of active carbon material feeding mouth side by pipeline respectively with the first inlet manifold, second
Inlet manifold and dry air house steward connect, and the gas outlet of active carbon material feeding mouth opposite side is all passed through
Pipeline connects exhaust main, and gas outlet is also connected with described second inlet manifold by pipeline, goes out
The steam inlet of QI KOU side all connects main steam range, described three activated carbon adsorption by pipeline
The bottom of tank all connects condenser by pipeline, and the bottom of condenser connects layering by pipeline
Groove, the side of layering groove connects back to closed cans by pipeline.
Organic gas recovery system of the present utility model, the inside of described eddy flow tower is provided with spray
Pipe, the end of shower connects water pump.
Organic gas recovery system of the present utility model, is provided with cigarette between described blower fan and surface cooler
Mist sensor.
Organic gas recovery system of the present utility model, the side of described second inlet manifold is provided with
Nitrogen header pipe, nitrogen header pipe is passed through the pipeline air inlet respectively with three absorbent charcoal adsorption tanks and is connected
Connect.
Organic gas recovery system of the present utility model, the top-right air vent of described condenser leads to
Crossing pipeline and connect gas-liquid separator, the bottom of gas-liquid separator is by pipeline with described layering groove even
Connect.
Compared with prior art the beneficial effects of the utility model are: organic gas of the present utility model
Body recovery system novel structure, the organic principle response rate of waste gas is up to more than 95%, recovery
Organic solvent can be directly used for producing, it is achieved that changing waste into resources；The cost recovery of organic solvent
Low, stable performance, service life is long.
Accompanying drawing explanation
Fig. 1 is the structural representation of the organic gas recovery system described in this utility model embodiment
Figure.
In figure:
1, eddy flow tower；2, surface cooler；3, absorbent charcoal adsorption tank；4, blower fan；5, activity
Carbon filter；6, the first inlet manifold；7, the second inlet manifold；8, dry air house steward；
9, active carbon material feeding mouth；10, air inlet；11, gas outlet；12, exhaust main；13、
Steam inlet；14, main steam range；15, condenser；16, layering groove；17, recycling can；
18, shower；19, water pump；20, nitrogen header pipe；21, gas-liquid separator.
Detailed description of the invention
Below in conjunction with the accompanying drawings and embodiment, detailed description of the invention of the present utility model is made further
Describe in detail.Following example are used for illustrating this utility model, but it is new to be not limited to this practicality
The scope of type.
As it is shown in figure 1, a kind of organic gas recovery system, including eddy flow tower 1, surface cooler 2
And three absorbent charcoal adsorption tanks being arranged side by side 3, connect between described eddy flow tower 1 and surface cooler 2
Giving a dinner for a visitor from afar machine 4, the end of surface cooler 2 connects active carbon filter 5, active carbon filter 5
Outlet is fixed with the first inlet manifold 6 being connected with three absorbent charcoal adsorption tanks 3, the first air inlet
The side of house steward 6 is provided with the second inlet manifold 7 and dry air house steward 8, and three activated carbons are inhaled
The top middle portion of attached tank 3 is equipped with active carbon material feeding mouth 9, entering of active carbon material feeding mouth 9 side
QI KOU 10 by pipeline respectively with first inlet manifold the 6, second inlet manifold 7 and be dried sky
Gas house steward 8 connects, and the gas outlet 11 of active carbon material feeding mouth 9 opposite side is all connected by pipeline
Exhaust main 12, gas outlet 11 is also connected with described second inlet manifold 7 by pipeline, goes out
The steam inlet 13 of QI KOU 11 side all by pipeline connect main steam range 14, described three
The bottom of absorbent charcoal adsorption tank 3 all connects condenser 15, the bottom of condenser 15 by pipeline
Connecting layering groove 16 by pipeline, the side of layering groove 16 connects back to closed cans 17 by pipeline.
Organic gas recovery system of the present utility model, the inside of described eddy flow tower 1 is provided with spray
Pipe 18, the end of shower 18 connects water pump 19.
Organic gas recovery system of the present utility model, sets between described blower fan 4 and surface cooler 2
There is Smoke Sensor.
Organic gas recovery system of the present utility model, the side of described second inlet manifold 7 sets
Have a nitrogen header pipe 20, nitrogen header pipe 20 by pipeline respectively with three absorbent charcoal adsorption tanks 3
Air inlet 10 connects.
Organic gas recovery system of the present utility model, the described top-right air vent of condenser 15
By pipeline connect gas-liquid separator 21, the bottom of gas-liquid separator 21 by pipeline with described point
Layer groove 16 connects.
Organic gas recovery system of the present utility model when specific works, described air inlet and
One inlet manifold, the second inlet manifold, dry air house steward, nitrogen header pipe connection pipeline on
Being equipped with valve, gas outlet also is provided with on the connection pipeline of the second inlet manifold and exhaust main
Valve, first waste gas inputted eddy flow tower, washed waste gas by shower.Eddy flow tower is defeated
After going out, the effect through blower fan enters surface cooler, the built-in circulating water pipe of surface cooler, utilizes recirculated water
Reduce EGT.Between blower fan and surface cooler, it is provided with Smoke Sensor, prevents sending out of fire
Raw.Active carbon filter, the built-in layer of active carbon of active carbon filter is entered after surface cooler output
Fiber, active carbon filter is arranged at the air outlet of surface cooler.After active carbon filter output
Enter the first inlet manifold, in the first inlet manifold respectively enters three absorbent charcoal adsorption tanks；
Absorbent charcoal adsorption tank crown center is active carbon material feeding mouth；Absorbent charcoal adsorption tank is provided with activated carbon
Packing layer, in the second inlet manifold enters other absorbent charcoal adsorption tanks, eventually passes aerofluxus
House steward's qualified discharge.When two absorbent charcoal adsorption tanks adsorb, another activated carbon adsorption
Tank is desorbed.During desorption, in absorbent charcoal adsorption tank, it is filled with steam by main steam range, enters
Row desorption；Desorption desorption liquid out enters in condenser by the bottom of absorbent charcoal adsorption tank,
Condenser built-in circulating water condensing pipe, desorption liquid enters layering groove, gas after condenser exports
Being entered gas-liquid separator by condenser exhaust gas mouth, gas-liquid separator separates liquid out enters and divides
Layer groove.Organic substance enters recycling can after layering groove output.Take off at absorbent charcoal adsorption tank
Time attached, discontinuity in absorbent charcoal adsorption tank, be filled with nitrogen, reduce in absorbent charcoal adsorption tank
The content of oxygen, prevents activated carbon from catching fire, and because absorbent charcoal adsorption tank is after desorption, activated carbon belongs to
In dampness, it is dried to ensure activated carbon adsorption performance to need activated carbon, de-
Attached complete after in absorbent charcoal adsorption tank, be filled with dry air by dry air house steward, ensure activity
Charcoal upper once adsorb time activated carbon absorption property.
The above is only preferred implementation of the present utility model, it is noted that for this skill
For the those of ordinary skill in art field, in the premise without departing from this utility model know-why
Under, it is also possible to making some improvement and modification, these improve and modification also should be regarded as this practicality newly
The protection domain of type.
Claims (5)
1. an organic gas recovery system, including eddy flow tower (1), surface cooler (2) and three
The individual absorbent charcoal adsorption tank (3) being arranged side by side, it is characterised in that: described eddy flow tower (1) with
Connecting fan (4) between surface cooler (2), the end of surface cooler (2) connects activated carbon and filters
Device (5), the outlet of active carbon filter (5) is fixed with and three absorbent charcoal adsorption tanks (3)
The first inlet manifold (6) connected, the side of the first inlet manifold (6) is provided with the second air inlet
House steward (7) and dry air house steward (8), the top middle portion of three absorbent charcoal adsorption tanks (3)
It is equipped with active carbon material feeding mouth (9), the air inlet (10) of active carbon material feeding mouth (9) side
By pipeline respectively with the first inlet manifold (6), the second inlet manifold (7) and dry air
House steward (8) connects, and the gas outlet (11) of active carbon material feeding mouth (9) opposite side is all by pipe
Road connects exhaust main (12), and gas outlet (11) are also total with described second air inlet by pipeline
Pipe (7) connects, and the steam inlet (13) of gas outlet (11) side is all connected by pipeline
Main steam range (14), the bottom of described three absorbent charcoal adsorption tanks (3) is all connected by pipeline
Condenser (15), the bottom of condenser (15) connects layering groove (16), layering by pipeline
The side of groove (16) connects back to closed cans (17) by pipeline.
Organic gas recovery system the most according to claim 1, it is characterised in that: institute
The inside stating eddy flow tower (1) is provided with shower (18), and the end of shower (18) connects water
Pump (19).
Organic gas recovery system the most according to claim 1, it is characterised in that: institute
State and be provided with Smoke Sensor between blower fan (4) and surface cooler (2).
Organic gas recovery system the most according to claim 1, it is characterised in that: institute
The side stating the second inlet manifold (7) is provided with nitrogen header pipe (20), and nitrogen header pipe (20) is led to
Piping is connected with the air inlet (10) of three absorbent charcoal adsorption tanks (3) respectively.
Organic gas recovery system the most according to claim 1, it is characterised in that: described
Condenser (15) top-right air vent connects gas-liquid separator (21), gas-liquid by pipeline
The bottom of separator (21) is connected with described layering groove (16) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620111252.6U CN205517197U (en) | 2016-02-03 | 2016-02-03 | Organic gas recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620111252.6U CN205517197U (en) | 2016-02-03 | 2016-02-03 | Organic gas recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205517197U true CN205517197U (en) | 2016-08-31 |
Family
ID=56776736
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620111252.6U Expired - Fee Related CN205517197U (en) | 2016-02-03 | 2016-02-03 | Organic gas recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205517197U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107899361A (en) * | 2017-09-22 | 2018-04-13 | 广东林顿重工股份有限公司 | A kind of waste gas recovering device |
| CN113350957A (en) * | 2021-07-06 | 2021-09-07 | 瑞燃(上海)环境工程技术有限公司 | Device and method for treating organic silicon waste gas |
-
2016
- 2016-02-03 CN CN201620111252.6U patent/CN205517197U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107899361A (en) * | 2017-09-22 | 2018-04-13 | 广东林顿重工股份有限公司 | A kind of waste gas recovering device |
| CN113350957A (en) * | 2021-07-06 | 2021-09-07 | 瑞燃(上海)环境工程技术有限公司 | Device and method for treating organic silicon waste gas |
| CN113350957B (en) * | 2021-07-06 | 2022-07-05 | 瑞燃(上海)环境工程技术有限公司 | Device and method for treating organic silicon waste gas |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202224049U (en) | Acid and hydrocarbon mixed waste gas treatment equipment | |
| CN208727090U (en) | A kind of fuel oil heating desulphurization denitration dust-extraction unit | |
| CN205517197U (en) | Organic gas recovery system | |
| CN102690689A (en) | Device and method for scrubbing and purifying coal gas | |
| CN204891537U (en) | Baffle reposition of redundant personnel laminar waste gas adsorption equipment | |
| CN206372683U (en) | A kind of sewage plant waste gas collection device | |
| CN104406184B (en) | A kind of Cremation Machine device for purifying and treating tail gas | |
| CN108187465A (en) | A kind of rubber house exhaust processing unit | |
| CN103232866B (en) | A fiber ball filler and a gas purification method using the same | |
| CN208449008U (en) | A kind of combined type organic waste-gas purification and recyclable device | |
| CN102151451B (en) | Multifunctional waste gas purification tower | |
| CN206560771U (en) | A kind of active carbon adsorption device | |
| CN203540266U (en) | Exhaust gas purifying tower | |
| CN205948570U (en) | Spray dust removal device of agriculture and forestry discarded object preparation active carbon | |
| CN205392059U (en) | Textile mill dust collecting equipment | |
| CN205084580U (en) | Toluene recovery unit | |
| CN202044872U (en) | Multifunctional waste gas purification tower | |
| CN205461763U (en) | Multi -functional waste gas purification is used in production of transparent polypropylene nucleating agent | |
| CN203810432U (en) | Flue gas processing device for coal fired boiler | |
| CN206008365U (en) | A kind of chemical industry uses environmental protection absorption tower | |
| CN208805074U (en) | A kind of flue gas waste heat recovery apparatus with dedusting function | |
| CN202700299U (en) | Water film dust-removing and benzene-removing device | |
| CN208097773U (en) | A kind of rubber house exhaust processing unit | |
| CN206688508U (en) | A kind of bio-trickling device and exhaust treatment system | |
| CN206751753U (en) | A kind of natural gas purification equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 315202 Ningbo, Zhenhai District, camel street, Yongping West Road, room 168, No. 205 (metro core area), No. Patentee after: Zhejiang Yi Long Environmental Services Co., Ltd. Address before: 315400 Ningbo Province, Zhenhai District, Zhuang City, the streets of the Dragon Road, No., building 528, No. 4 Patentee before: ZHEJIANG XIANGNIU ENVIRONMENTAL PROTECTION AND TECHNOLOGY DEVELOPMENT CO., LTD. |
|
| CP03 | Change of name, title or address | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20190203 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |