CN107940480A - A kind of coating waste gas incinerator - Google Patents
A kind of coating waste gas incinerator Download PDFInfo
- Publication number
- CN107940480A CN107940480A CN201711126308.0A CN201711126308A CN107940480A CN 107940480 A CN107940480 A CN 107940480A CN 201711126308 A CN201711126308 A CN 201711126308A CN 107940480 A CN107940480 A CN 107940480A
- Authority
- CN
- China
- Prior art keywords
- incinerator
- catalytic reactor
- waste gas
- coating waste
- catalytic
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
Abstract
The present invention relates to a kind of coating waste gas incinerator, the catalytic reactor being obliquely installed is installed in the incinerator, the lower left of the catalytic reactor is the entrance of incinerator, the surface of the catalytic reactor is the outlet of incinerator, and the right side of the catalytic reactor is equipped with two opposite burners.The area of the invention for setting inclined catalytic reactor to increase catalytic reactor in incinerator, improves the catalytic efficiency of catalytic reactor;Metal mesh is set in the top of catalytic reactor, metal mesh heat transfer block, be heated evenly, organic gas that can be in burning waste gas.
Description
Technical field
The present invention relates to waste gas pollution control and treatment apparatus field, more particularly to a kind of coating waste gas incinerator.
Background technology
VOC refers to that initial boiling point is less than or equal to 250 DEG C and can produce stimulation to visual perception under 101 .3kPa of standard atmospheric pressure
The organic compound of harm, since VOC generally exists with gaseous state, in order to handle the gas, generally using organic waste gas furnace
To burn;And the component of some VOC needs the temperature of higher that organic matter could be completely decomposed into harmless carbon dioxide and water,
That is superhigh temperature organic waste gas furnace;The existing most high temperature organic exhaust gas incinerator in China be subject to technology and cost due to being limited
System, its combustion catalysis is less efficient, effectively can not carry out sufficiently catalytic burning to exhaust gas;
Therefore, there is an urgent need for a kind of higher coating waste gas incinerator of efficiency of combustion.
The content of the invention
It is an object of the invention to overcome problem above existing in the prior art, there is provided a kind of coating waste gas incinerator;
To realize above-mentioned technical purpose and the technique effect, the present invention is achieved through the following technical solutions:
A kind of coating waste gas incinerator, is provided with the catalytic reactor being obliquely installed, the lower left of catalytic reactor in incinerator
For the entrance of incinerator, the surface of catalytic reactor is the outlet of incinerator, and the right side of catalytic reactor is equipped with two relatively
Burner;
Wherein, catalytic reactor include silicon-aluminum oxide be pressed into honeycomb support, coated in the oxygen on honeycomb support
The metallic catalyst changed aluminium thin layer, be deposited on microcrystalline state in alumina flake;
Wherein, one block of porous ceramic plate in parallel is equipped with the lower section of catalytic reactor, gas is uniformly dispersed;
Wherein, it is equipped with one piece of metal mesh in parallel in the top of catalytic reactor;
Wherein, the bottom of the incinerator side opposite with its entrance is equipped with a pure air input port, is passed through into incinerator
Pure air promotes waste gas catalytic combustion;
Wherein, be additionally provided with disposal box in incinerator and below catalytic reactor, in disposal box vertical direction by up to
Have dust bag;
The beneficial effects of the invention are as follows:The present invention sets inclined catalytic reactor to increase catalytic reactor in incinerator
Area, improve the catalytic efficiency of catalytic reactor;Catalytic reactor top set metal mesh, metal mesh heat transfer block, by
It is hot uniformly, organic gas that can be in burning waste gas.
Brief description of the drawings
Attached drawing described herein is used for providing a further understanding of the present invention, forms the part of the application, this hair
Bright schematic description and description is used to explain the present invention, does not form inappropriate limitation of the present invention;In the accompanying drawings:
Fig. 1 is the structure diagram of incinerator in the embodiment of the present invention.
Embodiment
It is below with reference to the accompanying drawings and in conjunction with the embodiments, next that the present invention will be described in detail;
As shown in Figure 1, a kind of coating waste gas incinerator, is provided with the catalytic reactor 26 being obliquely installed in incinerator 2, catalysis
The lower left of reactor 26 is the entrance 21 of incinerator 2, and the surface of catalytic reactor 26 is the outlet 22 of incinerator 2, catalysis
The right side of reactor 26 is equipped with two opposite burners 24;
During work, exhaust gas is entered inside incinerator 2 from 2 entrance 21 of incinerator, and is carried out by the catalytic reactor 26 of setting
Catalytic reaction, then carries out burning disposal so that will handle by the burner 24 set to the exhaust gas after catalytic reaction
Exhaust gas carry out high temperature and destroy carbonization by fire, to achieve the purpose that disinfection, finally from the outlet 22 of setting discharge gas;Pass through at the same time
The pure air input port 23 of setting supplements suitable air, to improve efficiency of combustion;
It can increase the area of catalytic reactor due to being provided with inclined catalytic reactor 26 in incinerator 2, improve catalysis
The catalytic efficiency of reactor;Metal mesh 27 is set in the top of catalytic reactor 26,27 heat transfer block of metal mesh, be heated evenly, energy
Part organic gas in enough burning waste gas;
In order to further optimize the implementation result of the present invention, in another embodiment of the invention, in foregoing teachings
On the basis of, above-mentioned catalytic reactor 26 include silicon-aluminum oxide be pressed into honeycomb support, coated in honeycomb support
On alumina flake, the metallic catalyst that is deposited on microcrystalline state in alumina flake;
In order to further optimize the implementation result of the present invention, in another embodiment of the invention, in foregoing teachings
On the basis of, it is above-mentioned to be equipped with one block of porous ceramic plate 25 in parallel in the lower section of catalytic reactor 26, disperse gas
Uniformly;
In order to further optimize the implementation result of the present invention, in another embodiment of the invention, in foregoing teachings
On the basis of, it is above-mentioned to be equipped with one piece of metal mesh in parallel in the top of catalytic reactor 26;
In order to further optimize the implementation result of the present invention, in another embodiment of the invention, in foregoing teachings
On the basis of, the side that the bottom of above-mentioned incinerator 2 is opposite with its entrance 21 is equipped with a pure air input port 23, to burning
Pure air is passed through in stove 2 promotes exhaust gas to be preferably catalyzed burning;
In order to further optimize the implementation result of the present invention, in another embodiment of the invention, in foregoing teachings
On the basis of, be additionally provided with disposal box in above-mentioned incinerator 2 and below catalytic reactor, in disposal box vertical direction by
Up to having dust bag;
Wherein, dust bag is made for high-temperature fibre;
Using above-mentioned preferred solution, dust bag collects the molecule carried in exhaust gas in the hot-fluid lower swing of incinerator, more
Add environmental protection;
Basic principle, main feature and the advantages of the present invention of the present invention has been shown and described above;The technical staff of the industry
It should be appreciated that the present invention is not limited to the above embodiments, the above embodiments and description only describe the present invention
Principle, without departing from the spirit and scope of the present invention, various changes and modifications of the present invention are possible, these change and
Improvement all fall within the protetion scope of the claimed invention.
Claims (6)
- A kind of 1. coating waste gas incinerator, it is characterised in that:The catalytic reactor being obliquely installed, institute are installed in the incinerator The lower left for stating catalytic reactor is the entrance of incinerator, and the surface of the catalytic reactor is the outlet of incinerator, described The right side of catalytic reactor is equipped with two opposite burners.
- 2. coating waste gas incinerator according to claim 1, it is characterised in that:The catalytic reactor includes silicon-alumina Honeycomb support that compound is pressed into, coated in the alumina flake on honeycomb support, with microcrystalline state be deposited on aluminium oxide Metallic catalyst in thin layer.
- 3. coating waste gas incinerator according to claim 1, it is characterised in that:It is equipped with the lower section of the catalytic reactor One block of porous ceramic plate in parallel, makes gas be uniformly dispersed.
- 4. coating waste gas incinerator according to claim 1, it is characterised in that:It is equipped with the top of the catalytic reactor One piece of metal mesh in parallel.
- 5. coating waste gas incinerator according to claim 1, it is characterised in that:The bottom of the incinerator and its entrance phase To side be equipped with a pure air input port, be passed through into incinerator pure air promote waste gas catalytic combustion.
- 6. coating waste gas incinerator according to claim 1, it is characterised in that:The incinerator is interior and is located at catalytic reaction Disposal box is additionally provided with below device, disposal box is interior to be from top to bottom equipped with dust bag in vertical direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711126308.0A CN107940480A (en) | 2017-11-15 | 2017-11-15 | A kind of coating waste gas incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711126308.0A CN107940480A (en) | 2017-11-15 | 2017-11-15 | A kind of coating waste gas incinerator |
Publications (1)
Publication Number | Publication Date |
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CN107940480A true CN107940480A (en) | 2018-04-20 |
Family
ID=61932187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201711126308.0A Pending CN107940480A (en) | 2017-11-15 | 2017-11-15 | A kind of coating waste gas incinerator |
Country Status (1)
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CN (1) | CN107940480A (en) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3329567A1 (en) * | 1983-08-16 | 1985-03-21 | Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck | Fossil combustion boiler with chemisorption inserts |
JPS6193305A (en) * | 1984-10-12 | 1986-05-12 | Matsushita Electric Ind Co Ltd | Liquid fuel burner |
WO2000003795A1 (en) * | 1998-07-13 | 2000-01-27 | Siemens Aktiengesellschaft | Static mixer |
CN105509073A (en) * | 2015-12-31 | 2016-04-20 | 张英华 | Blast furnace gas catalytic combustion equipment and method for purely combusting blast furnace gas |
CN205550043U (en) * | 2016-05-05 | 2016-09-07 | 武汉甲四方环保科技有限公司 | Combined type dust -containing waste gas purifier |
CN106885253A (en) * | 2017-02-21 | 2017-06-23 | 安徽海纳森环境科技有限公司 | A kind of burned waste gas processing unit |
-
2017
- 2017-11-15 CN CN201711126308.0A patent/CN107940480A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3329567A1 (en) * | 1983-08-16 | 1985-03-21 | Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck | Fossil combustion boiler with chemisorption inserts |
JPS6193305A (en) * | 1984-10-12 | 1986-05-12 | Matsushita Electric Ind Co Ltd | Liquid fuel burner |
WO2000003795A1 (en) * | 1998-07-13 | 2000-01-27 | Siemens Aktiengesellschaft | Static mixer |
CN105509073A (en) * | 2015-12-31 | 2016-04-20 | 张英华 | Blast furnace gas catalytic combustion equipment and method for purely combusting blast furnace gas |
CN205550043U (en) * | 2016-05-05 | 2016-09-07 | 武汉甲四方环保科技有限公司 | Combined type dust -containing waste gas purifier |
CN106885253A (en) * | 2017-02-21 | 2017-06-23 | 安徽海纳森环境科技有限公司 | A kind of burned waste gas processing unit |
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Application publication date: 20180420 |