CN204469501U - A kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas - Google Patents
A kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas Download PDFInfo
- Publication number
- CN204469501U CN204469501U CN201520093083.3U CN201520093083U CN204469501U CN 204469501 U CN204469501 U CN 204469501U CN 201520093083 U CN201520093083 U CN 201520093083U CN 204469501 U CN204469501 U CN 204469501U
- Authority
- CN
- China
- Prior art keywords
- adsorption
- adsorber rotor
- desorption
- cylindrical shell
- horizontal rotation
- 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.)
- Active
Links
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model discloses a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas, comprise cylindrical shell, annular adsorber rotor is provided with in cylindrical shell, dividing plate is provided with between cylindrical shell and adsorber rotor, space between cylindrical shell and adsorber rotor is at least separated out 3 isolated areas by described dividing plate, be respectively adsorption zone, desorption district and cooling zone, on described cylinder lateral wall, the position of corresponding adsorption zone is provided with adsorbed gas entrance, the inner side of described adsorber rotor is connected with adsorbed gas discharge line, on described cylinder lateral wall, the position in corresponding desorption district is provided with desorption gas entrance, the position in the corresponding desorption district, inner side of described adsorber rotor is connected with desorption gas discharge line, on described cylinder lateral wall, the position of corresponding cooling zone is provided with refrigerating gas outlet, refrigerating gas outlet is connected with adsorbed gas discharge line.The utility model can realize the thickening-purification technology of dusty gas, for low concentration gas process provides condition, has saved the energy.
Description
Technical field
The utility model relates to a kind of horizontal rotation apparatus with Adsorption Concentration organic exhaust gas function, belongs to VOCs treatment technical field.
Background technology
Traditional organic waste gas treatment method resolves into carbon dioxide and water after mainly the organic component in waste gas being heated to uniform temperature, thus the organic component reduced in waste gas is to the pollution of environment.This process is again an exothermic process, when waste gas reaches finite concentration, waste gas decomposition caused heat release can maintain this process continue carry out.And will be difficult many for the process of low concentration gas.In low concentration gas, content of organics is lower, combustion heat release is less, shortage of heat after burning, to maintain the burning of follow-up waste gas, in order to maintain organic decomposition, needs the heat that extra increase is a large amount of, the burning of the fuel such as electrical heating, natural gas, diesel oil, kerosene is such as utilized to provide energy, maintain organic last decomposition, because the consumption of this process to the energy is a lasting process, so, bring larger economic loss to exhaust-gas treatment person, also waste mass energy simultaneously.
Utility model content
Based on above-mentioned technical problem, the utility model provides a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas.
The technical solution that the utility model adopts is:
A kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas, comprise cylindrical shell, adsorber rotor is provided with in cylindrical shell, the ring-shaped section and ring-shaped of described adsorber rotor, dividing plate is provided with between cylindrical shell and adsorber rotor, space between cylindrical shell and adsorber rotor is at least separated out 3 isolated areas by described dividing plate, be respectively adsorption zone, desorption district and cooling zone, on described cylinder lateral wall, the position of corresponding adsorption zone is provided with adsorbed gas entrance, the inner side of described adsorber rotor is connected with adsorbed gas discharge line, on described cylinder lateral wall, the position in corresponding desorption district is provided with desorption gas entrance, the position in the corresponding desorption district, inner side of described adsorber rotor is connected with desorption gas discharge line, on described cylinder lateral wall, the position of corresponding cooling zone is provided with refrigerating gas outlet, refrigerating gas outlet is connected with adsorbed gas discharge line.
Preferably, described cylindrical shell is vertically arranged, and described adsorber rotor is axial arranged along cylindrical shell.
Preferably, the boundary of described adsorption zone, desorption district and cooling zone is provided with hermetically-sealed construction, described hermetically-sealed construction comprises elastic packing adhesive tape and elastic clip, elastic packing adhesive tape comprises end head and afterbody, the boundary close contact of described end head and adsorption zone, desorption district and cooling zone, described afterbody is fixed by elastic clip.
Preferably, described end head is column construction, and cross section is rounded or oval.
Preferably, described end head is hollow structure.
Preferably, between described adsorption zone and desorption district, between adsorption zone and cooling zone, and be provided with isolated area between desorption district and cooling zone.
Preferably, described adsorber rotor is in transmission connection by sprocket wheel or belt and driving control device.
Preferably, described driving control device is connected with automatic control system.
Advantageous Effects of the present utility model is:
(1) the utility model can realize the thickening-purification technology of dusty gas, for low concentration gas process provides condition, has saved the energy.
(2) the utility model adopts and vertically arranges cylindrical shell, and in cylindrical shell, arrange the mode of annular adsorber rotor, and for the Adsorption Concentration realizing low concentration gas provides a kind of new version, compact in design is reasonable.
(3) hermetically-sealed construction in the utility model, the good waste gas vibration of having isolated each interval, improves treatment effeciency and the cocnentration factor of waste gas.
Accompanying drawing explanation
Below in conjunction with accompanying drawing and detailed description of the invention, the utility model is described in further detail:
Fig. 1 is structural principle schematic diagram of the present utility model;
Fig. 2 is top view of the present utility model.
In figure: 1-cylindrical shell, 2-adsorber rotor, 3-dividing plate, 4-adsorption zone, 5-desorption district, 6-cooling zone, 7-adsorbed gas entrance, 8-adsorbed gas discharge line, 9-desorption gas entrance, 10-desorption gas discharge line, 11-refrigerating gas exports, 12-motor, 13-base.
Detailed description of the invention
By reference to the accompanying drawings, a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas, comprise the vertical cylindrical shell 1 arranged, axially adsorber rotor 2 is provided with along it in cylindrical shell 1 inside, the ring-shaped section and ring-shaped of described adsorber rotor 2, adsorber rotor 2 can adopt the adsorbents such as the molecular sieve with straight-through porous shape structure.Between cylindrical shell 1 and adsorber rotor 2, be provided with multiple dividing plate 3, described dividing plate 3 will be separated out 3 isolated areas between cylindrical shell 1 and adsorber rotor 2, is respectively adsorption zone 4, desorption district 5 and cooling zone 6.On described cylinder lateral wall, the position of corresponding adsorption zone 4 is provided with adsorbed gas entrance 7, the inner side of described adsorber rotor 2 is connected with adsorbed gas discharge line 8, low concentration gas enters adsorption zone through adsorbed gas entrance 7, and after adsorber rotor Adsorption Concentration, discharge through adsorbed gas discharge line 8.On described cylinder lateral wall, the position in corresponding desorption district 5 is provided with desorption gas entrance 9, the position in the corresponding desorption district, inner side of described adsorber rotor 2 is connected with desorption gas discharge line 10, elevated temperature desorption gas enters desorption district through desorption gas entrance 9, organic pollution on adsorber rotor is separated out, form high-concentration waste gas, and discharge through desorption gas discharge line 8.On described cylinder lateral wall, the position of corresponding cooling zone 6 is provided with refrigerating gas outlet 11, and refrigerating gas outlet 11 is connected with adsorbed gas discharge line 8, namely uses the gas in adsorbed gas discharge line 8 to carry out cooling regeneration to adsorber rotor.
Above-mentioned adsorber rotor 2 is in transmission connection by sprocket wheel or belt and motor 12, and adsorber rotor drives running by motor 12, successively through adsorption zone 4, desorption district 5 and cooling zone 6.Above-mentioned motor 12 is connected with automatic control system, and automatic control system can regulate arbitrarily the rotating speed of adsorber rotor 2 according to technological requirement.
As to further improvement of the utility model, the boundary of above-mentioned adsorption zone, desorption district and cooling zone is provided with hermetically-sealed construction, described hermetically-sealed construction comprises elastic packing adhesive tape and elastic clip, elastic packing adhesive tape comprises end head and afterbody, the boundary close contact of described end head and adsorption zone, desorption district and cooling zone, described afterbody is fixed by elastic clip.Described end head is cylindrical hollow structure, and cross section is rounded or oval.
Further, in order to strengthen the sealing effectiveness of each operation interval, also between described adsorption zone and desorption district, between adsorption zone and cooling zone, and between desorption district and cooling zone, an isolated area can be all set.
Below the course of work of the present utility model is briefly explained:
During work, the low concentration gas containing organic pollution enters adsorption zone by adsorbed gas entrance 7, and after adsorber rotor 2, succession is by the molecular sieve adsorption in adsorber rotor 2, and clean gas is discharged by adsorbed gas discharge line 8.Along with the continuous rotation of adsorber rotor 2, in adsorber rotor 2, Adsorption Concentration has the moieties of organic pollution sieve to enter desorption district, in desorption district, separate out under the elevated temperature desorption gas effect that organic exhaust gas in molecular sieve enters in desorption gas entrance 9, form the waste gas of high concentration, and discharge through desorption gas discharge line 10.Moieties sieve subsequently on adsorber rotor 2 rotates to cooling zone, and under the effect of cold wind (clean gas in adsorbed gas discharge line 8), be cooled to room temperature, molecular sieve has also recovered adsorption capacity.Along with the continuous rotation of adsorber rotor 2, adsorber rotor 2 Middle molecule sieve is constantly carrying out adsorption and desorption, cooling, and adsorption process again, achieves the uninterrupted purification of organic exhaust gas, concentrated.
Certainly; above-mentioned explanation is not to restriction of the present utility model; the utility model is also not limited in above-mentioned citing, the change that those skilled in the art make in essential scope of the present utility model, remodeling, interpolation or replacement, also should belong to protection domain of the present utility model.
Claims (8)
1. the horizontal rotation apparatus for Adsorption Concentration organic exhaust gas, it is characterized in that: comprise cylindrical shell, adsorber rotor is provided with in cylindrical shell, the ring-shaped section and ring-shaped of described adsorber rotor, dividing plate is provided with between cylindrical shell and adsorber rotor, space between cylindrical shell and adsorber rotor is at least separated out 3 isolated areas by described dividing plate, be respectively adsorption zone, desorption district and cooling zone, on described cylinder lateral wall, the position of corresponding adsorption zone is provided with adsorbed gas entrance, the inner side of described adsorber rotor is connected with adsorbed gas discharge line, on described cylinder lateral wall, the position in corresponding desorption district is provided with desorption gas entrance, the position in the corresponding desorption district, inner side of described adsorber rotor is connected with desorption gas discharge line, on described cylinder lateral wall, the position of corresponding cooling zone is provided with refrigerating gas outlet, refrigerating gas outlet is connected with adsorbed gas discharge line.
2. a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas according to claim 1, it is characterized in that: described cylindrical shell is vertically arranged, described adsorber rotor is axial arranged along cylindrical shell.
3. a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas according to claim 1, it is characterized in that: the boundary of described adsorption zone, desorption district and cooling zone is provided with hermetically-sealed construction, described hermetically-sealed construction comprises elastic packing adhesive tape and elastic clip, elastic packing adhesive tape comprises end head and afterbody, the boundary close contact of described end head and adsorption zone, desorption district and cooling zone, described afterbody is fixed by elastic clip.
4. a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas according to claim 3, is characterized in that: described end head is column construction, and cross section is rounded or oval.
5. a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas according to claim 3, is characterized in that: described end head is hollow structure.
6. a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas according to claim 1, is characterized in that: between described adsorption zone and desorption district, between adsorption zone and cooling zone, and is provided with isolated area between desorption district and cooling zone.
7. a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas according to claim 1, is characterized in that: described adsorber rotor is in transmission connection by sprocket wheel or belt and driving control device.
8. a kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas according to claim 7, is characterized in that: described driving control device is connected with automatic control system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520093083.3U CN204469501U (en) | 2015-02-10 | 2015-02-10 | A kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520093083.3U CN204469501U (en) | 2015-02-10 | 2015-02-10 | A kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204469501U true CN204469501U (en) | 2015-07-15 |
Family
ID=53625237
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520093083.3U Active CN204469501U (en) | 2015-02-10 | 2015-02-10 | A kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204469501U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731473A (en) * | 2017-03-16 | 2017-05-31 | 上海兰宝环保科技有限公司 | Industrial organic waste-gas purification device |
| CN108187448A (en) * | 2018-02-27 | 2018-06-22 | 江苏安琪尔废气净化有限公司 | A kind of highly enriched organic waste gas concentrating device and method light-dutyer than high temperature resistant |
| CN109069981A (en) * | 2016-03-28 | 2018-12-21 | 东洋纺株式会社 | Absorbing treatment device |
| CN110465159A (en) * | 2019-07-25 | 2019-11-19 | 江苏苏净集团有限公司 | A kind of processing exhaust gas adsorption runner device |
-
2015
- 2015-02-10 CN CN201520093083.3U patent/CN204469501U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109069981A (en) * | 2016-03-28 | 2018-12-21 | 东洋纺株式会社 | Absorbing treatment device |
| CN106731473A (en) * | 2017-03-16 | 2017-05-31 | 上海兰宝环保科技有限公司 | Industrial organic waste-gas purification device |
| CN108187448A (en) * | 2018-02-27 | 2018-06-22 | 江苏安琪尔废气净化有限公司 | A kind of highly enriched organic waste gas concentrating device and method light-dutyer than high temperature resistant |
| CN108187448B (en) * | 2018-02-27 | 2023-12-15 | 江苏安琪尔废气净化有限公司 | High-concentration-ratio high-temperature-resistant light organic waste gas concentration device and method |
| CN110465159A (en) * | 2019-07-25 | 2019-11-19 | 江苏苏净集团有限公司 | A kind of processing exhaust gas adsorption runner device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| AU2014373727B2 (en) | Rotating multi-monolith bed movement system for removing CO2 from the atmosphere | |
| CN204469501U (en) | A kind of horizontal rotation apparatus for Adsorption Concentration organic exhaust gas | |
| CN103764254B (en) | For the system and method that the integrated form adsorbed gas of burning gases separates | |
| CN201578875U (en) | Low-temperature condensation and adsorption recovery device containing high-concentration low-level aromatic hydrocarbon exhaust gas | |
| CN203790800U (en) | Waste gas purification device with online regenerated adsorbent | |
| CN204247047U (en) | Organic exhaust gas adsorption concentrates catalytic combustion and low-temperature plasma coupling purification system | |
| KR102579864B1 (en) | Parallel pipe type gas adsorption concentrator | |
| CN201295583Y (en) | Adsorption and catalysis integration device | |
| CN203591682U (en) | Honeycomb activated carbon adsorption rotating wheel | |
| CN105854512A (en) | Activated carbon fiber adsorption device | |
| CN202942782U (en) | Waste gas adsorption filter | |
| CN210814549U (en) | Control type low-consumption blowing regeneration dryer | |
| CN104190205A (en) | Exhaust gas recovery cycle working method and device | |
| CN204469500U (en) | For the pulsating whirligig of Adsorption Concentration organic exhaust gas | |
| CN103120882A (en) | Automatic control method for cycling operation of organic waste gas recovery adsorption tank | |
| CN204469499U (en) | A kind of emission-control equipment for Adsorption Concentration | |
| CN103159580B (en) | Method of purifying and extracting methane in waste landfill gas | |
| CN203443264U (en) | Device for extracting methane liquid from purified garbage landfill gas | |
| CN202921142U (en) | Vertical fixed bed adsorber | |
| CN205288010U (en) | Novel organic waste gas purifier treatment equipment | |
| CN103752296A (en) | Device and method for regeneration of powdered activated carbon | |
| CN103353207A (en) | Device for purifying methane liquid from purified landfill gas | |
| CN103933829B (en) | Air-treatment absorption rotary wheel device | |
| CN203002177U (en) | Coke oven gas deep purification pretreatment system for direct-fired machine power generation | |
| CN104667704A (en) | Pulse-type rotating device for adsorbing concentrated organic waste gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |