CN201894909U - Volatile organic matter treatment and catalytic reaction tank - Google Patents
Volatile organic matter treatment and catalytic reaction tank Download PDFInfo
- Publication number
- CN201894909U CN201894909U CN2010205695396U CN201020569539U CN201894909U CN 201894909 U CN201894909 U CN 201894909U CN 2010205695396 U CN2010205695396 U CN 2010205695396U CN 201020569539 U CN201020569539 U CN 201020569539U CN 201894909 U CN201894909 U CN 201894909U
- Authority
- CN
- China
- Prior art keywords
- retort body
- heater
- accommodation space
- treatment
- catalytic reactor
- 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 - Lifetime
Links
Images
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The utility model discloses a volatile organic matter treatment and catalytic reaction tank which comprises a reaction tank body provided with an air inlet tube and an air outlet tube, wherein the reaction tank also comprises a catalyst installed in the reaction tank body; and at least one group of heaters used for heating air entering the reaction tank body are arranged on the outer wall or at the inner part of the reaction tank body. The volatile organic matter treatment and catalytic reaction tank can carry out effective treatment and purification on the air entering a testing bin, effectively improve the testing precision and better meet the demand for the testing environment.
Description
Technical field
The utility model relates to a kind of being used for entering the TREATMENT OF VOCs catalytic reactor that airborne volatile organic matter in the test cabin carries out effective treatment and purification.
Background technology
Along with improving constantly of people's living standard, people also are greatly improved to the requirement of environmental quality, especially to the environmental index of living environment, are not subjected to the injury of noxious materials such as formaldehyde with the health that ensures the people.And a lot of indoor materials and product all contain noxious materials such as formaldehyde, for to ensure that the people's is healthy, need the release rate and the release characteristics of noxious materials such as indoor material and the contained benzene of product, toluene, formaldehyde be detected, especially detect in certain hot environment, thereby obtain qualified indoor material and product, make people that a good living environment be arranged.Need introduce air from the external world in that the release rate of noxious materials such as indoor material and the contained benzene of product, toluene, formaldehyde and release characteristics are detected,, need handle the volatile organic matter of introducing air in order to ensure the cleaning of introducing air.
The utility model content
The purpose of this utility model is to overcome above-mentioned defective in the prior art: providing a kind of can carry out effective treatment and purification to the air that enters in the test cabin, effectively improves test accuracy, satisfies the TREATMENT OF VOCs catalytic reactor of experimental enviroment needs better.
For achieving the above object, the technical scheme that the utility model provides is as follows: construct a kind of TREATMENT OF VOCs catalytic reactor, comprise the retort body, the retort body is provided with air intake duct, air escape pipe, also comprise being installed in the intrinsic catalyst of retort, be equiped with at least one group of heater that the air that enters the retort body is carried out heat temperature raising in the outer wall or the inside of described retort body.
The beneficial effect of TREATMENT OF VOCs catalytic reactor described in the utility model is: by constructing a retort body, the retort body is provided with air intake duct, air escape pipe, be equiped with catalyst in the retort body, the outer wall of described retort body or inside are equiped with at least one group of heater that the air that enters the retort body is carried out heat temperature raising.Can carry out effective treatment and purification to the air that enters in the test cabin, effectively improve test accuracy, satisfy the experimental enviroment needs better.
Below in conjunction with drawings and Examples TREATMENT OF VOCs catalytic reactor described in the utility model is described further:
Description of drawings
Fig. 1 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented one structural representation;
Fig. 2 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented two structural representation;
Fig. 3 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented three structural representation;
Fig. 4 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented four structural representation;
Fig. 5 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented five structural representation;
Fig. 6 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented six structural representation;
Fig. 7 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented seven structural representation;
Fig. 8 is that the utility model TREATMENT OF VOCs catalytic reactor is implemented eight perspective structure schematic diagram.
The specific embodiment
Below the most preferred embodiment of TREATMENT OF VOCs catalytic reactor described in the utility model, therefore do not limit protection domain of the present utility model.
Implement one, with reference to Fig. 1, a kind of TREATMENT OF VOCs catalytic reactor is provided, comprise retort body 1, retort body 1 is provided with air intake duct 2, air escape pipe 3, also comprise the catalyst 4 that is installed in the retort body 1, outer wall or inside at described retort body 1 are equiped with at least one group of at least one group of heater 5 that the air that enters retort body 1 is carried out heat temperature raising, air enters retort body 1 and has an effect with catalyst 4, airborne volatile organic matter is removed, thereby reached the purpose that purifies air.
Described heater 5 is fixed on retort body 1 outer wall, and this heater 5 is mica baffle heater, stainless steel outer sleeve heater, heating cartridge heater, electromagnetic heater.
Described and heater 5 is cast into one with retort body 1, and cast material is metal or alloy.
Be equiped with the temperature sensor that is used for detected temperatures and control heater heating on the described heater 5 or in the retort body 1.
There is the insulation material insulation described retort body 1 outside.
Described air escape pipe 3 is equiped with orifice plate, filter screen, is used to stop that catalysis visit agent 4 enters in the retort body 1.
Implement two, with reference to Fig. 2, described catalyst 4 is filled in the full entire reaction jar body 1, and heater 5 is arranged on retort body 1 outer wall, and described air intake duct 2 adheres to or is wrapped on retort body 1 outer wall, can carry out preheating to air.
Implement three, with reference to Fig. 3, be separated into first accommodation space 7, second accommodation space 8 in the described retort body 1, be equiped with heater 5 in first accommodation space 7, second accommodation space 8 is filled full catalyst 4, air intake duct 2 is arranged on first accommodation space, 7 ends, and air escape pipe 3 is arranged on second accommodation space, 8 ends.
Implement four, with reference to Fig. 4, be separated into first accommodation space 7, second accommodation space 8 in the described retort body 1, the nonmetal filler 9 of wire netting filler, metallic object filler or heatproof is housed in first accommodation space 7, second accommodation space 8 is filled full catalyst 4, air intake duct 2 is arranged on first accommodation space, 7 ends, and air escape pipe 3 is arranged on second accommodation space, 8 ends, and heater 5 is arranged on retort body 1 outer wall.
Implement five, with reference to Fig. 5, be separated into first accommodation space 7, second accommodation space 8 in the described retort body 1, in first accommodation space 7 porous metal bodies 10 is housed, second accommodation space 8 is filled full catalyst 4, air intake duct 2 is arranged on first accommodation space, 7 ends, and air escape pipe 3 is arranged on second accommodation space, 8 ends, and heater 5 is arranged on retort body 1 outer wall.
Implement six, with reference to Fig. 6, described catalyst 4 is filled in the full entire reaction jar body 1, and heater 5 is arranged in the retort body 1, and air intake duct 2 is arranged on retort body 1 one ends, and air escape pipe 3 is arranged on retort body 1 other end.
Implement seven, with reference to Fig. 7, described catalyst 4 is filled in the full entire reaction jar body 1, heater 5 is arranged in the retort body 1, air intake duct 2 is arranged on retort body 1 sidewall, and air escape pipe 3 is installed in the retort body 1, and stretches out in retort body 1.
Implement eight, with reference to Fig. 8, described retort body 1 is a metal derby, on this metal derby, offer lateral opening 11, vertically perforate 12, described lateral opening 11, vertical perforate 12 connect mutually, and form one and have air intake duct 2, air escape pipe 3 air ducts, described catalyst 4 is filled and should also be offered the perforate 13 that several are used to install heater 5 on this metal derby in air duct.
The foregoing description is the utility model preferred implementation; but embodiment of the present utility model is not restricted to the described embodiments; other any do not deviate from change, the modification done under spiritual essence of the present utility model and the principle, substitutes, combination, simplify; all should be the substitute mode of equivalence, be included within the protection domain of the present utility model.
Claims (10)
1. TREATMENT OF VOCs catalytic reactor, comprise retort body (1), retort body (1) is provided with air intake duct (2), air escape pipe (3), it is characterized in that, also comprise the catalyst (4) that is installed in the retort body (1), be equiped with at least one group of at least one group of heater (5) that the air that enters retort body (1) is carried out heat temperature raising in the outer wall or the inside of described retort body (1).
2. TREATMENT OF VOCs catalytic reactor according to claim 1, it is characterized in that, described heater (5) is fixed on retort body (1) outer wall, and this heater (5) is mica baffle heater, stainless steel outer sleeve heater, heating cartridge heater, electromagnetic heater.
3. TREATMENT OF VOCs catalytic reactor according to claim 2 is characterized in that, described and heater (5) is cast into one with retort body (1).
4. TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that, described heater (5) upward or in the retort body (1) is equiped with the temperature sensor that is used for detected temperatures.
5. TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that, there is the insulation material insulation described retort body (1) outside.
6. TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that, described air intake duct (2) adheres to or is wrapped on retort body (1) outer wall.
7. TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that, described air escape pipe (3) is equiped with orifice plate, filter screen.
8. TREATMENT OF VOCs catalytic reactor according to claim 1, it is characterized in that, described retort body (1) is a metal derby, on this metal derby, offer lateral opening (11), vertically perforate (12), described lateral opening (11), vertically perforate (12) perforation mutually, and form one and have air inlet (2), gas outlet (3) air duct, described catalyst (4) is filled and should also be offered several perforates that is used to install heater (5) (13) on this metal derby in air duct.
9. TREATMENT OF VOCs catalytic reactor according to claim 1, it is characterized in that, be separated into first accommodation space (7) in the described retort body (1), second accommodation space (8), first accommodation space is equipped with the wire netting filler in (7), metallic object filler or nonmetal heatproof filler (9), second accommodation space (8) is filled full catalyst (4), air intake duct (2) is arranged on first accommodation space (7) end, air escape pipe (3) is arranged on second accommodation space (8) end, and heater (5) is arranged on retort body (1) outer wall.
10. TREATMENT OF VOCs catalytic reactor according to claim 1, it is characterized in that, be separated into first accommodation space (7), second accommodation space (8) in the described retort body (1), porous metal bodies (10) is housed in first accommodation space (7), second accommodation space (8) is filled full catalyst (4), air intake duct (2) is arranged on first accommodation space (7) end, air escape pipe (3) is arranged on second accommodation space (8) end, and heater (5) is arranged on retort body (1) outer wall.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205695396U CN201894909U (en) | 2010-10-20 | 2010-10-20 | Volatile organic matter treatment and catalytic reaction tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205695396U CN201894909U (en) | 2010-10-20 | 2010-10-20 | Volatile organic matter treatment and catalytic reaction tank |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201894909U true CN201894909U (en) | 2011-07-13 |
Family
ID=44252828
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010205695396U Expired - Lifetime CN201894909U (en) | 2010-10-20 | 2010-10-20 | Volatile organic matter treatment and catalytic reaction tank |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201894909U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102000500A (en) * | 2010-10-20 | 2011-04-06 | 东莞市升微机电设备科技有限公司 | Retort for processing and catalyzing volatile organic compound |
CN102961963A (en) * | 2012-11-28 | 2013-03-13 | 南京金美镓业有限公司 | High-concentration nitrogen oxide waste gas catalytic decomposing device |
-
2010
- 2010-10-20 CN CN2010205695396U patent/CN201894909U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102000500A (en) * | 2010-10-20 | 2011-04-06 | 东莞市升微机电设备科技有限公司 | Retort for processing and catalyzing volatile organic compound |
CN102000500B (en) * | 2010-10-20 | 2013-01-23 | 东莞市升微机电设备科技有限公司 | Retort for processing and catalyzing volatile organic compound |
CN102961963A (en) * | 2012-11-28 | 2013-03-13 | 南京金美镓业有限公司 | High-concentration nitrogen oxide waste gas catalytic decomposing device |
CN102961963B (en) * | 2012-11-28 | 2015-02-04 | 南京金美镓业有限公司 | High-concentration nitrogen oxide waste gas catalytic decomposing method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101692025B (en) | Test system for detecting volatile organic compounds | |
CN201517972U (en) | Test system for detecting volatile organics | |
CN201894909U (en) | Volatile organic matter treatment and catalytic reaction tank | |
CN107398142A (en) | A kind of air cleaning facility of filter core free of replacement | |
CN102000500B (en) | Retort for processing and catalyzing volatile organic compound | |
CN101530743B (en) | Oil smoke purifier applicable to downdraft kitchen ventilator | |
CN202161919U (en) | Catalytic reaction tank for large flow volatile organics treatment | |
CN107975854A (en) | Internal circulation oil smoke purification integrated system | |
CN206777243U (en) | A kind of tappasaki | |
CN208012919U (en) | A kind of opium volume production cigarette device of more material settling out production cigarettes | |
CN204758439U (en) | A kitchen environmental detection set for arrange lampblack absorber | |
CN209020159U (en) | A kind of efficiency of waste gas processing system | |
CN102350213A (en) | Catalytic reaction tank for processing large-flow volatile organic matter | |
CN206103645U (en) | High -efficient carbon fiber adsorbed case | |
CN107218662A (en) | The VMC and manufacture method of a kind of atmosphere pollution | |
CN210045060U (en) | Three-phase multi-medium catalytic oxidation tower for purifying and treating asphalt smoke waste gas | |
CN208465599U (en) | A kind of emission-control equipment | |
CN208504557U (en) | Photocatalyst fan coil | |
CN207413114U (en) | A kind of waste gas purification apparatus of family expenses kitchen waste disposer | |
CN106369619B (en) | A kind of use for laboratory heavy metal super-enriched plant combustion furnace | |
CN104307304A (en) | Parallel activated carbon adsorption box | |
CN201740739U (en) | Nox converter | |
CN206996239U (en) | A kind of karl Fischer reagent toxic gas filter of improved structure | |
CN205372683U (en) | High -quality oil smoke machine aviation baffle | |
CN206414876U (en) | A kind of filter core, filtration system for being used to remove biomass gasification tar |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20110713 Effective date of abandoning: 20130306 |
|
RGAV | Abandon patent right to avoid regrant |