CN102350213A - Catalytic reaction tank for processing large-flow volatile organic matter - Google Patents
Catalytic reaction tank for processing large-flow volatile organic matter Download PDFInfo
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- CN102350213A CN102350213A CN2011101887150A CN201110188715A CN102350213A CN 102350213 A CN102350213 A CN 102350213A CN 2011101887150 A CN2011101887150 A CN 2011101887150A CN 201110188715 A CN201110188715 A CN 201110188715A CN 102350213 A CN102350213 A CN 102350213A
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- heater
- retort body
- reaction tank
- big flow
- catalytic reactor
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Abstract
The invention discloses a catalytic reaction tank for processing a large-flow volatile organic matter. The catalytic reaction tank comprises a reaction tank body, an air inlet pipe and an air outlet pipe which are arranged on the reaction tank body and a catalyst arranged in the reaction tank body; at least one group of heaters for heating air entering the reaction tank body are arranged on the outer wall or inside of the reaction tank body; one end of the air inlet pipe extends into the reaction tank body, and a sleeve pipe is sleeved at one end of the air inlet pipe; and an exhaust hole is formed at the front end of the sleeve pipe. By the catalytic reaction tank, air entering in a test bin can be purified effectively, the test accuracy can be improved effectively, and particularly the requirement of test environment for purification of the large-flow air can be better met.
Description
Technical field
The present invention relates to a kind of big flow TREATMENT OF VOCs catalytic reactor that is used for the airborne volatile organic matter in the entering test cabin is carried 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, do not receive 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 arranged.To indoor material and the contained benzene of product; Toluene; The release rate of noxious materials such as formaldehyde and release characteristics detect need introduce air from the external world; Cleaning in order to ensure the introducing air; Need handle the volatile organic matter of introducing air; And traditional its air of TREATMENT OF VOCs catalytic reactor is not heated in retort fully; Can not fully react with the retort inner catalyst; Especially in the time of need carrying out treatment and purification to the air of big flow; Just can not effectively remove airborne volatile organic matter, not reach the purpose of air being carried out treatment and purification.
Summary of the invention
The objective of the invention 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 gets in the test cabin, effectively improves test accuracy, especially can satisfy the big flow TREATMENT OF VOCs catalytic reactor that the air of big flow is carried out the experimental enviroment needs of treatment and purification better.
For realizing above-mentioned purpose; Technical scheme provided by the invention is following: construct a kind of big flow TREATMENT OF VOCs catalytic reactor; Comprise the retort body; Be installed in air intake duct, air escape pipe on the retort body; Be installed in the intrinsic catalyst of retort; Outer wall or inside at said retort body are equiped with at least one group of at least one group of heater that the air that gets into the retort body is carried out heat temperature raising; Said air intake duct one end stretches in the retort body and is arranged with a sleeve pipe, and the front end of this sleeve pipe offers steam vent.
The beneficial effect of big flow TREATMENT OF VOCs catalytic reactor according to the invention is: through constructing a retort body; The retort body is provided with air intake duct, air escape pipe; In the retort body, be equiped with catalyst; The outer wall of said retort body or inside are equiped with at least one group of heater that the air that gets into the retort body is carried out heat temperature raising; Said air intake duct one end stretches in the retort body and is arranged with a sleeve pipe, and the front end of this sleeve pipe offers steam vent.The air of pending purification heats the back first at air intake duct and in air intake duct inflow sleeve pipe, carries out post bake; The air of pending purification is through carry out chemical reaction with catalyst after the post bake again in the steam vent inflow retort body of sleeve pipe front end; Because the air of pending purification has obtained sufficient heating; Can effectively remove the airborne volatile organic matter of pending purification; Thereby can carry out effective treatment and purification to the air that gets in the test cabin, effectively improve test accuracy, especially can satisfy the experimental enviroment needs that the air of big flow carried out treatment and purification better.
Below in conjunction with accompanying drawing and embodiment big flow TREATMENT OF VOCs catalytic reactor of the present invention is described further:
Description of drawings
Fig. 1 is that the big flow TREATMENT OF VOCs of the present invention catalytic reactor is implemented one structural representation;
Fig. 2 is that the big flow TREATMENT OF VOCs of the present invention catalytic reactor is implemented two structural representation.
The specific embodiment
Below the most preferred embodiment of big flow TREATMENT OF VOCs catalytic reactor according to the invention, therefore do not limit protection scope of the present invention.
Implement one; With reference to Fig. 1; A kind of big flow TREATMENT OF VOCs catalytic reactor is provided; Comprise retort body 1; Be installed in air intake duct 2, air escape pipe 3 on the retort body 1; Be installed in the catalyst 4 in the retort body 1; Outer wall or inside at said retort body 1 are equiped with at least one group of at least one group of heater 5 that the air that gets into retort body 1 is carried out heat temperature raising; Said air intake duct 2 one ends stretch in the retort body 1 and are arranged with a sleeve pipe 6, and the front end of this sleeve pipe 6 offers steam vent 7.
Said 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.
Said 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 control heater heating 5 on the said heater 5 or in the retort body 1.
There is the insulation material insulation said retort body 1 outside.
Said air escape pipe 3 is equiped with orifice plate, filter screen, is used to stop in the catalysis visit agent 4 outflow retort bodies 1.
Implement two, with reference to Fig. 2, said heater 5 is fixed on retort body 1 inside, and this heater 5 is immerging metal tube heater or METAL HEATING PROCESS silk.
The foregoing description is a preferred implementation of the present invention; But embodiment of the present invention is not restricted to the described embodiments; Other any do not deviate from change, the modification done under spirit of the present invention and the principle, substitutes, combination, simplify; All should be the substitute mode of equivalence, be included within protection scope of the present invention.
Claims (7)
1. one kind big flow TREATMENT OF VOCs catalytic reactor; Comprise retort body (1); Be installed in the air intake duct (2) on the retort body (1); Air escape pipe (3); Be installed in the catalyst (4) in the retort body (1); Outer wall or inside at said retort body (1) are equiped with at least one group of at least one group of heater (5) that the air that gets into retort body (1) is carried out heat temperature raising; It is characterized in that; Said air intake duct (2) one ends stretch in the retort body (1) and are arranged with a sleeve pipe (6), and the front end of this sleeve pipe (6) offers steam vent (7).
2. big flow TREATMENT OF VOCs catalytic reactor according to claim 1; It is characterized in that; Said 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. big flow TREATMENT OF VOCs catalytic reactor according to claim 2 is characterized in that, said heater (5) is cast into one with retort body (1).
4. big flow TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that, is equiped with the temperature sensor that is used for detected temperatures control heater heating (5) on the said heater (5) or in the retort body (1).
5. big flow TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that, there is the insulation material insulation said retort body (1) outside.
6. big flow TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that said air escape pipe (3) is equiped with orifice plate, filter screen.
7. big flow TREATMENT OF VOCs catalytic reactor according to claim 1 is characterized in that said heater (5) is fixed on retort body (1) inside, and this heater (5) is immerging metal tube heater or METAL HEATING PROCESS silk.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101887150A CN102350213A (en) | 2011-07-07 | 2011-07-07 | Catalytic reaction tank for processing large-flow volatile organic matter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101887150A CN102350213A (en) | 2011-07-07 | 2011-07-07 | Catalytic reaction tank for processing large-flow volatile organic matter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102350213A true CN102350213A (en) | 2012-02-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011101887150A Pending CN102350213A (en) | 2011-07-07 | 2011-07-07 | Catalytic reaction tank for processing large-flow volatile organic matter |
Country Status (1)
| Country | Link |
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| CN (1) | CN102350213A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002126701A (en) * | 2000-10-27 | 2002-05-08 | Sanyo Electric Co Ltd | Organic matter treating device |
| CN2566174Y (en) * | 2002-08-18 | 2003-08-13 | 曲庆生 | Electromagnetic heat exchanger |
| 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 |
| CN202161919U (en) * | 2011-07-07 | 2012-03-14 | 东莞市升微机电设备科技有限公司 | Catalytic reaction tank for large flow volatile organics treatment |
-
2011
- 2011-07-07 CN CN2011101887150A patent/CN102350213A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002126701A (en) * | 2000-10-27 | 2002-05-08 | Sanyo Electric Co Ltd | Organic matter treating device |
| CN2566174Y (en) * | 2002-08-18 | 2003-08-13 | 曲庆生 | Electromagnetic heat exchanger |
| 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 |
| CN202161919U (en) * | 2011-07-07 | 2012-03-14 | 东莞市升微机电设备科技有限公司 | Catalytic reaction tank for large flow volatile organics treatment |
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| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20120215 |