CN206304534U - Charcoal absorption condenses emission-control equipment - Google Patents
Charcoal absorption condenses emission-control equipment Download PDFInfo
- Publication number
- CN206304534U CN206304534U CN201621342413.9U CN201621342413U CN206304534U CN 206304534 U CN206304534 U CN 206304534U CN 201621342413 U CN201621342413 U CN 201621342413U CN 206304534 U CN206304534 U CN 206304534U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- connects
- condenser
- absorbent charcoal
- tank
- 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 provides a kind of charcoal absorption condensation emission-control equipment, waste gas pipeline road connects a gas buffer tank, waste gas enters two lower ends of absorbent charcoal adsorption tank by being divided to two branch roads after gas buffer tank, PAN-ACF bed is set in the absorbent charcoal adsorption tank, the lower end of two absorbent charcoal adsorption tanks connects circulating fan by pipeline, the circulating fan connects spark arrester, the spark arrester is sequentially connected precooler and condenser by pipeline afterwards, the condenser connects two upper ends of absorbent charcoal adsorption tank by pipeline, the upper end of two absorbent charcoal adsorption tanks sets exhaust fan by pipeline, exhaust fan connects floss hole;Adsorbed using fiber charcoal, with significant economic benefit and environmental benefit;It is integrated with condenser, the adsorbent bed of precooler function can be heated up or be lowered the temperature to activated carbon in a short time, improves adsorption and desorption speed, efficiency increase.
Description
Technical field
The utility model belongs to technical field of waste gas treatment, more particularly, to a kind of charcoal absorption condensation exhaust-gas treatment dress
Put.
Background technology
Prevention and cure of pollution problem containing VOC (Volatile organic compounds, volatile organic matter) waste gas is gradually
It is taken seriously, Introduced From Abroad abatement equipment has that investment is big, operating cost is high, and domestic traditional handicraft has technology and falls
Afterwards, the low problem of fluctuation of service, efficiency, therefore urgently research and develop new processing unit.Activated carbon of the present utility model is inhaled
Attached condensation emission-control equipment based on adsorbing 2 condensations and reclaim principle, using the new of integrated heater and cooler function
Adsorbent bed fibre active carbon, while waste gas is purified, has reclaimed substantial amounts of VOC solvent, Environmental Inputs is generated preferably
Economic benefit and environmental benefit.
Utility model content
The purpose of this utility model is to provide a kind of charcoal absorption condensation emission-control equipment, is adapted at industrial waste gas
Reason.
The technical solution of the utility model is:Waste gas pipeline road connects a gas buffer tank, and waste gas is by gas buffer
It is divided to two branch roads to enter two lower ends of absorbent charcoal adsorption tank after tank, PAN-ACF bed is set in the absorbent charcoal adsorption tank,
PAN-ACF bed sets multilayer adsorption layer, and cooler and heater, two lower ends of absorbent charcoal adsorption tank are provided between layers
Circulating fan is connected by pipeline, the circulating fan connects spark arrester, and the spark arrester is sequentially connected pre- by pipeline afterwards
Cooler and condenser, the condenser connect two upper ends of absorbent charcoal adsorption tank, two absorbent charcoal adsorption tanks by pipeline
Upper end by pipeline set exhaust fan, exhaust fan connection floss hole.
Above-mentioned charcoal absorption condensation emission-control equipment, wherein:Jet chimney is set on two absorbent charcoal adsorption tanks
And cooling water pipeline.
Above-mentioned charcoal absorption condensation emission-control equipment, wherein:Chilled brine pipeline, institute are set on the condenser
State and cooling water pipeline is set on precooler.
Above-mentioned charcoal absorption condensation emission-control equipment, wherein:The condenser, the lower section of precooler are set back
Receive liquid storage tank, recovered liquid storage tank platoon waterpipe.
There is the utility model effect to be:
1) high concentration VOC waste gas is adsorbed using fiber charcoal, with significant economic benefit and environmental benefit;It is integrated with condensation
Device, the adsorbent bed of precooler function can be heated up or be lowered the temperature to activated carbon in a short time, put forward adsorption and desorption speed
Height, efficiency increase;2) present treatment device is applied to high concentration (1 × more than 10-3), the VOC of small air quantity (10 below 000m3Ph)
Waste gas pollution control and treatment.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure:
The precooling of 1 gas buffer tank, 2 fibrous carbon adsorbent bed, 3 recovered liquid storage tank, 4 circulating fan, 5 spark arrester, 6 condenser 7
But the drainage pipeline of 8 air exhauster of device, 9 chilled brine pipeline, 10 jet chimney, 11 cooling water pipeline 12
Specific embodiment
The utility model is elaborated below in conjunction with the accompanying drawings.
Charcoal absorption of the present utility model condenses emission-control equipment, and waste gas pipeline road connects a gas buffer tank 1,
Waste gas by being divided to two branch roads to enter the lower ends of two absorbent charcoal adsorption tanks after gas buffer tank 1, in the absorbent charcoal adsorption tank
PAN-ACF bed 2 is set, to obtain preferably absorption and desorption efficiency, it is desirable to which adsorbent bed heating, cooling speed is fast, empty in bed
Gas, N2 residual volumes are small, and the lifting of de-adsorption cycle gas VOC concentration is fast.PAN-ACF bed 2 sets multilayer adsorption layer, between layers
Cooler and heater are provided with, installation is tightly beaten, PAN-ACF 2 remaining space insides of bed are small, and VOC concentration is carried quickly when making desorption
Rise.Two lower ends of absorbent charcoal adsorption tank connect circulating fan 4 by pipeline, and the circulating fan 4 connects spark arrester 5, afterwards
The spark arrester 5 is sequentially connected precooler 7 and condenser 6 by pipeline, and the condenser 6 connects two activity by pipeline
The upper end of charcoal adsorption tanks, two upper ends of absorbent charcoal adsorption tank set exhaust fan 8, the connection discharge of exhaust fan 8 by pipeline
Mouthful.
Jet chimney 10 and cooling water pipeline 11 are set on two absorbent charcoal adsorption tanks;Freezing is set on the condenser 6
Brine pipeline 9, sets cooling water pipeline 11 on the precooler 7;The condenser 6, the lower section of precooler 7 set and reclaim
Liquid storage tank 3, the platoon waterpipe 12 of recovered liquid storage tank 3.
Desorption process, heater and circulating fan 4, make system heat comprehensively, as activated carbon temperature is improved, VOC
Gradually parse, VOC concentration is also improved constantly in recyclegas.First pre-cooled but device 7 of gas of the discharge of PAN-ACF bed 2
Cooling, then condensed device 6 makes VOC condensation recovery get off, and the heated device of gas heats up and returns to the heating solution of PAN-ACF bed 2 afterwards
Analysis activated carbon, desorption process does not introduce fresh air, and desorption cocnentration factor is higher.
One embodiment of the present utility model has been described in detail above, but the content is only of the present utility model
Preferred embodiment, it is impossible to be considered as limiting practical range of the present utility model.It is all to be made according to present utility model application scope
Impartial change with improve etc., all should still belong within patent covering scope of the present utility model.
Claims (4)
1. a kind of charcoal absorption condenses emission-control equipment, it is characterised in that:Waste gas pipeline road connects a gas buffer tank,
Waste gas sets by being divided to two branch roads to enter two lower ends of absorbent charcoal adsorption tank after gas buffer tank in the absorbent charcoal adsorption tank
PAN-ACF bed is put, PAN-ACF bed sets multilayer adsorption layer, cooler and heater, two activity are provided between layers
The lower end of charcoal adsorption tanks connects circulating fan by pipeline, and the circulating fan connects spark arrester, and the spark arrester passes through afterwards
Pipeline is sequentially connected precooler and condenser, and the condenser connects two upper ends of absorbent charcoal adsorption tank, two by pipeline
The upper end of individual absorbent charcoal adsorption tank sets exhaust fan, exhaust fan connection floss hole by pipeline.
2. charcoal absorption as claimed in claim 1 condenses emission-control equipment, it is characterised in that:Two absorbent charcoal adsorption tanks
It is upper that jet chimney and cooling water pipeline are set.
3. a kind of charcoal absorption as claimed in claim 2 condenses emission-control equipment, it is characterised in that:On the condenser
Chilled brine pipeline is set, cooling water pipeline is set on the precooler.
4. a kind of charcoal absorption as claimed in claim 3 condenses emission-control equipment, it is characterised in that:The condenser,
The lower section of precooler sets recovered liquid storage tank, recovered liquid storage tank platoon waterpipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621342413.9U CN206304534U (en) | 2016-12-08 | 2016-12-08 | Charcoal absorption condenses emission-control equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621342413.9U CN206304534U (en) | 2016-12-08 | 2016-12-08 | Charcoal absorption condenses emission-control equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206304534U true CN206304534U (en) | 2017-07-07 |
Family
ID=59249951
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621342413.9U Expired - Fee Related CN206304534U (en) | 2016-12-08 | 2016-12-08 | Charcoal absorption condenses emission-control equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206304534U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108786419A (en) * | 2018-06-23 | 2018-11-13 | 台州帆环保设备科技有限公司 | A variety of exhaust gas total systems |
CN109985485A (en) * | 2019-04-29 | 2019-07-09 | 南京兆博环保科技有限公司 | A kind of device and method of high concentrations of gas absorbing, recovering and purifying |
-
2016
- 2016-12-08 CN CN201621342413.9U patent/CN206304534U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108786419A (en) * | 2018-06-23 | 2018-11-13 | 台州帆环保设备科技有限公司 | A variety of exhaust gas total systems |
CN109985485A (en) * | 2019-04-29 | 2019-07-09 | 南京兆博环保科技有限公司 | A kind of device and method of high concentrations of gas absorbing, recovering and purifying |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103736359B (en) | A kind of adsorption-desorption reclaims device and the technique of VOC | |
CN104801146B (en) | Device and process for recovering volatile organic gas | |
CN103463932B (en) | Method and device for treating and recycling organic exhaust gas with low concentration and large air volume | |
CN109045925A (en) | A kind of VOCs waste gas recovery processing unit and method | |
CN101301558A (en) | Activated carbon fiber organic solvent recovery novel technique using nitrogen as desorption medium | |
CN203540289U (en) | Treating and recovering device of organic waste gas with low concentration and large air volume | |
CN106807178A (en) | A kind of adsorbent absorption, the device and method of hot drying gas desorption treatment organic exhaust gas | |
CN106621697A (en) | Efficient solvent recycling device | |
CN206152550U (en) | Exhaust treatment device in pyridine production | |
CN206304534U (en) | Charcoal absorption condenses emission-control equipment | |
CN206325361U (en) | A kind of cloth-bag type NACF purifier | |
CN205925337U (en) | Second grade sorption recovery system | |
CN208574439U (en) | Atmosphere volume low-concentration organic exhaust gas recycling and processing device | |
CN208406512U (en) | A kind of organic waste gas concentrating oxidation integrating device | |
CN206642549U (en) | Multicomponent VOC recycling and processing device | |
CN211537120U (en) | Organic waste gas purification device and system adopting thermal nitrogen desorption | |
CN108079766A (en) | A kind of low concentration big flow organic exhaust gas closed loop multistage retracting device and recovery method | |
CN205109291U (en) | Organic gas's processing apparatus | |
CN204768144U (en) | Adsorption recovery device of organic waste gas | |
CN207221631U (en) | A kind of Adsorption Concentration equipment for organic exhaust gas | |
CN105771300A (en) | Oil and gas recovery system | |
CN105861026A (en) | Residual oily gas recycling and treatment device and treatment method | |
CN205323264U (en) | Condensation flow controller | |
CN214320175U (en) | High-temperature nitrogen desorption and condensation recovery device | |
CN205516888U (en) | Organic waste gas graphite alkene sorption recovery device |
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: 20170707 Termination date: 20201208 |