CN204911239U - Organic waste gas integration clarification plant - Google Patents
Organic waste gas integration clarification plant Download PDFInfo
- Publication number
- CN204911239U CN204911239U CN201520721609.8U CN201520721609U CN204911239U CN 204911239 U CN204911239 U CN 204911239U CN 201520721609 U CN201520721609 U CN 201520721609U CN 204911239 U CN204911239 U CN 204911239U
- Authority
- CN
- China
- Prior art keywords
- catalyst
- reaction
- exhaust gas
- reaction vessel
- reactant liquor
- 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
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The utility model belongs to the technical field of the organic waste gas purification treatment technique and specifically relates to an organic waste gas integration clarification plant. This organic waste gas integration clarification plant is used for purification of organic waste gas, including casing, reaction vessel, free radical emergence system, reaction wall and reaction liquid atomizing system, the casing is a confined space, the system takes place and locates with the reaction wall for the free radical inside the reaction vessel, the reaction wall is located the free radical and takes place the system top, inside reaction vessel located the casing, organic waste gas was inside through input pipeline input reaction vessel, free radical emergence system pass through communicating pipe with the input pipeline is linked together, the reaction is equipped with multiple at least a catalyst on the wall, reaction liquid atomizing system locates the reaction is square on the wall, and the organic waste gas after the purification passes through output pipeline and exports outside the casing.
Description
Technical field
The utility model relates to organic waste-gas purification processing technology field, specifically a kind of organic exhaust gas integration cleaning equipment.
Background technology
The removal of tradition organic gas uses charcoal absorption to remove, and adsorbing saturated active carbon can regenerate use, but after repeatedly using, active carbon can thoroughly saturatedly cannot regenerate, and these active carbons can cause certain harm as hazardous waste to environment.The simultaneously process of active carbon, regeneration, replacing can produce larger operating cost, in these processes, exhaust-gas treatment stays cool, therefore exhaust treatment efficiency is not high enough, and it is stable not often to change active carbon reaction effect, moreover, charcoal treatment equipment needs certain time of contact, and can produce pollution to air when carbon-coating penetrates.This system utilizes free-radical oxidation, and treatment effect is thorough, and treatment effect is more stable simultaneously, and therefore, when the equal treatment scale of this equipment, floor space is less, and equipment investment is less.Meanwhile, and the treatment effect of this equipment is stable can not produce Similar Problems.
Utility model content
The utility model provides the organic exhaust gas integration cleaning equipment that a kind of structure is simple, the reaction time is short, treatment effeciency is high, treatment effect is stable.
The utility model is achieved through the following technical solutions:
A kind of organic exhaust gas integration cleaning equipment, for cleaning organic waste gas, comprise housing, reaction vessel, radical generating system, reaction wall and reactant liquor atomization system, described housing is a closed space, described reaction vessel interior is located at by described radical generating system and reaction wall, described reaction wall is positioned at above radical generating system, enclosure interior is located at by described reaction vessel, organic exhaust gas inputs reaction vessel interior by input channel, described radical generating system is connected with described input channel by connecting pipe, described reaction wall is provided with multiple at least one catalyst, described reactant liquor atomization system is located at above described reaction wall, organic exhaust gas after purification outputs to outside housing by output channel, catalyst on described reaction wall from below to up layering is arranged, described catalyst cupport is in catalyst carrier, and be located on reaction wall by catalyst carrier filler, described reaction wall is divided into the first catalyst filling layer, the second catalyst filling layer and the 3rd catalyst filling layer from below to up.
Catalyst on described first catalyst filling layer, the second catalyst filling layer and the 3rd catalyst filling layer is different.
Described input channel is provided with filtration system, and it is outside that described filtration system is positioned at described reaction vessel.
Described output channel is provided with blower fan, and it is outside that described blower fan is positioned at described reaction vessel.
Described reactant liquor atomization system comprises reactant liquor pipeline and reactant liquor shower nozzle, and described reactant liquor lower end of duct is connected with described reaction vessel bottom, and described reactant liquor shower nozzle is located at described reactant liquor pipeline upper end, and is positioned at above described reaction wall.
The beneficial effect that the utility model brings is:
In the utility model, described organic exhaust gas integration cleaning equipment utilizes free-radical oxidation, and the reaction time is short, and treatment effect is better, and treatment effect is thorough, and maintenance management is convenient and simple, and treatment effect is more stable simultaneously, and floor space is less, and equipment investment is less.
The oxidation reaction of free radical is usually used in wastewater treatment at present, and this equipment is that the pioneering ozone catalytic generation free radical that utilizes at normal temperatures and pressures directly processes organic exhaust gas.
The carrier filler of this organic exhaust gas integration cleaning equipment has salient feature, in order to reduce the reaction time, stop secondary pollution, the catalysis system of this reactor is heterogeneous catalysis system, and the catalyst simultaneously according to the different catalysts packing layer packing layer load of reaction stage of development is not identical yet.
Reactant liquor main component is water, recycles within the system, reduces secondary pollution as far as possible.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Fig. 1 is the structural representation of organic exhaust gas integration cleaning equipment first embodiment described in the utility model.
Fig. 2 is the structural representation of organic exhaust gas integration cleaning equipment second embodiment described in the utility model.
The label that in figure, component names is corresponding is as follows:
1, housing; 2, reaction vessel; 3, radical generating system; 4, wall is reacted; 5, input channel; 6, connecting pipe; 7, output channel; 8, the first catalyst carrier filler; 9, the second catalyst carrier filler; 10, the 3rd catalyst carrier filler; 11, filtration system; 12, blower fan; 13, reactant liquor pipeline; 14, reactant liquor shower nozzle.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described in further detail:
Embodiment one:
As the embodiment of organic exhaust gas integration cleaning equipment described in the utility model, as shown in Figure 1, for cleaning organic waste gas, described organic exhaust gas integration cleaning equipment comprises housing 1, reaction vessel 2, radical generating system 3, reaction wall 4 and reactant liquor atomization system, described housing 1 is a closed space, it is inner that described reaction vessel 2 is located at by described radical generating system 3 and reaction wall 4, described reaction wall 4 is positioned at above radical generating system 3, it is inner that housing 1 is located at by described reaction vessel 2, it is inner that organic exhaust gas inputs reaction vessel 2 by input channel 5, described radical generating system 3 is connected with described input channel 5 by connecting pipe 6, described reaction wall 4 is provided with catalyst, described reactant liquor atomization system is located at above described reaction wall 4, organic exhaust gas after purification outputs to outside housing 1 by output channel 7, catalyst on described reaction wall 4 from below to up layering is arranged, described catalyst cupport is in catalyst carrier, and be located on reaction wall by catalyst carrier filler, described reaction wall is divided into the first catalyst filling layer 8 from below to up, second catalyst filling layer 9 and the 3rd catalyst filling layer 10, described first catalyst filling layer 8, catalyst on second catalyst filling layer 9 and the 3rd catalyst filling 10 layers is different.Described housing 1 major function is that formation confined space prevents free radical and organic exhaust gas from revealing; Described reaction wall 4 is as the Main Function place of purification, organic exhaust gas is thoroughly purified through this region, reaction wall 4 provides support for catalyst carrier filler, simultaneous reactions liquid, catalyst, free radical, machine waste gas this formation gas-solid-liquid interface, and by interface occur free-radical oxidation reaction; Described catalyst carrier filler Main Function is catalysis radical reaction, and the catalyst of load on filler is different according to the difference of the stage of reaction; In order to reduce the reaction time, stop secondary pollution, the catalysis system of this equipment is heterogeneous catalysis system, and the catalyst simultaneously according to the different catalysts packing layer load of reaction stage of development is not identical yet.
In the present embodiment, described output channel 7 is provided with blower fan 12, and it is outside that described blower fan 12 is positioned at described reaction vessel 2.Described blower fan 12 plays the effect that organic exhaust gas is circulated from below to up, can discharge smoothly after entering purification.
In the present embodiment, described reactant liquor atomization system comprises reactant liquor pipeline 13 and reactant liquor shower nozzle 14, described reactant liquor pipeline 13 lower end is connected with described reaction vessel 2 bottom, and described reactant liquor shower nozzle 14 is located at described reactant liquor pipeline 13 upper end, and is positioned at above described reaction wall 4.Reactant liquor is atomized, is conducive to the abundant haptoreaction of reactant liquor, catalyst, free radical and organic exhaust gas, reduces the resistance to mass tranfer at gas-solid-liquid interface.
Embodiment two:
As the embodiment of organic exhaust gas integration cleaning equipment described in the utility model, as shown in Figure 2, be: in the present embodiment with the difference of embodiment one, described input channel 5 is provided with filtration system 11, and it is outside that described filtration system 11 is positioned at described reaction vessel 2.Be provided with the operation adopting filtration system 11 to filter to the organic exhaust gas entering housing 1 before described step (1), the organic exhaust gas after filtration enters reaction vessel 2 again.When matching filtration system 11 containing needing during more particulate pollutant in organic exhaust gas, described filtration system 11 can remove the particulate pollutant in organic exhaust gas.
In the present embodiment, all the other structures and beneficial effect are all consistent with embodiment one, repeat no longer one by one here.
Embodiment three:
As the embodiment of organic exhaust gas integration cleaning equipment described in the utility model, be: in the present embodiment with the difference of embodiment one, described input channel 5 is provided with filtration system 11, and it is outside that described filtration system 11 is positioned at described reaction vessel 2.Be provided with the operation adopting filtration system 11 to filter to the organic exhaust gas entering housing 1 before described step (1), the organic exhaust gas after filtration enters reaction vessel 2 again.
In the present embodiment, all the other structures and beneficial effect are all consistent with embodiment one, repeat no longer one by one here.
More than describe preferred embodiment of the present utility model in detail.Should be appreciated that those of ordinary skill in the art just can make many modifications and variations according to design of the present utility model without the need to creative work.Therefore; the technical scheme that any amendment that all technical staff are in the art done by logical analysis, reasoning, or a limited experiment on the basis of existing technology according to design of the present utility model, equivalent replacement, improvement etc. obtain, all should by the determined protection domain of claims.
Claims (5)
1. an organic exhaust gas integration cleaning equipment, for cleaning organic waste gas, it is characterized in that comprising housing, reaction vessel, radical generating system, reaction wall and reactant liquor atomization system, described housing is a closed space, described reaction vessel interior is located at by described radical generating system and reaction wall, described reaction wall is positioned at above radical generating system, enclosure interior is located at by described reaction vessel, organic exhaust gas inputs reaction vessel interior by input channel, described radical generating system is connected with described input channel by connecting pipe, described reaction wall is provided with multiple at least one catalyst, described reactant liquor atomization system is located at above described reaction wall, organic exhaust gas after purification outputs to outside housing by output channel, catalyst on described reaction wall from below to up layering is arranged, described catalyst cupport is in catalyst carrier, and be located on reaction wall by catalyst carrier filler, described reaction wall is divided into the first catalyst filling layer, the second catalyst filling layer and the 3rd catalyst filling layer from below to up.
2. organic exhaust gas integration cleaning equipment as claimed in claim 1, is characterized in that the catalyst on described first catalyst filling layer, the second catalyst filling layer and the 3rd catalyst filling layer is different.
3. organic exhaust gas integration cleaning equipment as claimed in claim 1, is characterized in that described input channel is provided with filtration system, and it is outside that described filtration system is positioned at described reaction vessel.
4. organic exhaust gas integration cleaning equipment as claimed in claim 1, is characterized in that described output channel is provided with blower fan, and it is outside that described blower fan is positioned at described reaction vessel.
5. organic exhaust gas integration cleaning equipment as claimed in claim 1, it is characterized in that described reactant liquor atomization system comprises reactant liquor pipeline and reactant liquor shower nozzle, described reactant liquor lower end of duct is connected with described reaction vessel bottom, described reactant liquor shower nozzle is located at described reactant liquor pipeline upper end, and is positioned at above described reaction wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520721609.8U CN204911239U (en) | 2015-09-15 | 2015-09-15 | Organic waste gas integration clarification plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520721609.8U CN204911239U (en) | 2015-09-15 | 2015-09-15 | Organic waste gas integration clarification plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204911239U true CN204911239U (en) | 2015-12-30 |
Family
ID=54960425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520721609.8U Expired - Fee Related CN204911239U (en) | 2015-09-15 | 2015-09-15 | Organic waste gas integration clarification plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204911239U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105056759A (en) * | 2015-09-15 | 2015-11-18 | 钱培玉 | Organic waste gas integral purification equipment |
-
2015
- 2015-09-15 CN CN201520721609.8U patent/CN204911239U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105056759A (en) * | 2015-09-15 | 2015-11-18 | 钱培玉 | Organic waste gas integral purification equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105521705A (en) | Method for treating organic waste gas through low-temperature plasma concerted catalysis | |
| CN101391177B (en) | Gas purification method of low concentration organic compound | |
| CN203556243U (en) | Industrial organic waste gas processing device | |
| CN100421769C (en) | Method for unwanted exhaust gas purification and dedicated apparatus | |
| CN205627430U (en) | Dedicated high -efficient environmental protection tail gas processing apparatus of factory sprays paint | |
| CN203043799U (en) | Acid mist purification tower | |
| CN203648389U (en) | Combined device for treating high-temperature and high-concentration organic waste gas by catalytic oxidation | |
| CN103230743B (en) | A kind of nitrogen oxide tail gas emission method | |
| CN203610046U (en) | Denitration catalysis filter device of dust remover | |
| CN203307143U (en) | Catalytic oxidation wastewater treatment device | |
| CN204911239U (en) | Organic waste gas integration clarification plant | |
| CN205760609U (en) | A kind of device for low-temperature plasma synergistic catalysis treatment organic exhaust gas | |
| CN101322916B (en) | Sulfur-containing compound gas cleaning filter medium device and method as well as used catalyst adsorption material thereof | |
| CN206082107U (en) | Industry organic waste gas purification device | |
| CN112807962A (en) | Chemical waste gas treatment system | |
| CN205164465U (en) | Low temperature plasma complete set exhaust -gas treatment equipment | |
| CN111266006A (en) | Integrated combined purifier | |
| CN216377482U (en) | Ozone recycling system | |
| CN212091693U (en) | Integrated combined purifier | |
| CN113318582A (en) | Process for adsorbing, desorbing and catalytically oxidizing VOCs (volatile organic compounds) by using activated carbon in pharmaceutical industry | |
| CN105056759A (en) | Organic waste gas integral purification equipment | |
| CN107986578A (en) | The biogas hydrogen manufacturing circulatory system and technique of a kind of PTA sewage disposals | |
| CN210699502U (en) | Industrial waste gas light catalytic oxidation treatment facility | |
| CN204768082U (en) | Multistage catalysis exhaust gas purification device | |
| CN103557056A (en) | Microbe purification device for purifying automobile exhaust |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| CB03 | Change of inventor or designer information |
Inventor after: Sun Jian Inventor before: Qian Peiyu |
|
| COR | Change of bibliographic data | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170303 Address after: 223814 Qixia Road, Suqian Industrial Park, Suqian, Jiangsu, No. 22, No. Patentee after: Suqian Fu Zheng Environmental Technology Co. Ltd. Address before: 314501 Zhejiang province Tongxiang city Wuzhen Town Village first Dai No. 8 Patentee before: Qian Peiyu |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151230 Termination date: 20170915 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |