CN207661804U - A kind of heat accumulating type tar disposition burner - Google Patents
A kind of heat accumulating type tar disposition burner Download PDFInfo
- Publication number
- CN207661804U CN207661804U CN201721790978.8U CN201721790978U CN207661804U CN 207661804 U CN207661804 U CN 207661804U CN 201721790978 U CN201721790978 U CN 201721790978U CN 207661804 U CN207661804 U CN 207661804U
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- CN
- China
- Prior art keywords
- cylinder
- tar
- gas pipeline
- catalysis net
- heat accumulating
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- 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.)
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Abstract
A kind of heat accumulating type tar disposition burner, including cylinder, catalytic thermal storage ball, catalysis net, gas pipeline, reticular structure is wrapped up outside the catalytic thermal storage ball, the catalysis net is located at inner barrel with gas pipeline, catalysis net top is connected with gas pipeline lower part, gas pipeline is connected through cylinder top with the cylinder external world, the catalysis net lower part is connected through cylinder with the cylinder external world, the reticular structure is that same coke tar cracking is catalyzed material composition with catalysis net, and the catalytic thermal storage bead is constituted with coke tar cracking catalysis material.The utility model is although simple in structure, but deft design, can efficiently use calory burning, removes the tar mixed in fuel gas.
Description
Technical field
The utility model is related to a kind of combustion apparatus, and in particular to a kind of combustion apparatus that can handle tar in combustion gas.
Background technology
During the processing of stalk integrated gasification and its process similarity, the combustible gas of institute's output includes a certain amount of coke
Oil, in this case tar be thoroughly mixed with fuel gas in gaseous state.
Tar ingredients are complicated, and processing is difficult, if not handling tar, directly burn, tar can not decompose, after discharge
Condense into liquid again when less than 200 DEG C, the tar of liquid is in black viscous liquid, is easy mixed with other ash contents and water
Aggregation is closed, blocks follow-up air duct or burning appliance, tiny coke tar particles will produce the particles such as carbon black in burning, to rear
Afterflame gas causes very big damage using equipment, and can form black smoke after combustion gas discharge pollutes.
The energy of tar accounts for about the 10% of gross energy, if being expelled directly out the gasification efficiency that can reduce the processing of stalk integrated gasification.
Kind of a mode is mainly the following to the processing of tar at present:
Physical partition method:First tar is converted to liquid from gaseous state, by the method washing or filter by tar from gas
Then middle separation is used as waste to handle, on the one hand this method wastes the energy of tar, and still further aspect tar processing is improper
It can cause seriously to pollute
Catalystic pyrolysis:Enter cat-cracker with the combustible gas of tar after gasification, carry tar at this time can
Combustion gas can be reduced to 600 DEG C, and external heat source keeps cat-cracker at 750 ~ 900 DEG C, the catalyst in cat-cracker
Under the action of so that catalytic cracking of tar reaches 99% or more, and this method system is complicated, and pyrolysis furnace interior conduit easily blocks, fortune
Row requires high.
Invention content
The utility model proposes a kind of heat accumulating type tar to dispose burner, and simple in structure, deft design can efficiently use
Calory burning removes the tar mixed in fuel gas.
The utility model solves the problems, such as that background content is proposed by the following technical programs:
Including:Reticular structure is wrapped up in cylinder, catalytic thermal storage ball, catalysis net, gas pipeline, the catalytic thermal storage ball outside,
The catalysis net is located at inner barrel with gas pipeline, and catalysis net top is connected with gas pipeline lower part, and gas pipeline runs through cylinder
Body top is connected with the cylinder external world, and the catalysis net lower part is connected through cylinder with the cylinder external world, the reticular structure and catalysis
Net is that same coke tar cracking is catalyzed material composition, and the catalytic thermal storage bead is constituted with coke tar cracking catalysis material.
The cylinder side top is equipped with air inlet.
The inner barrel is embedded with refractory brick, and thermal insulation material is wrapped up outside cylinder.
The cylinder body bottom is equipped with admission line, and described admission line one end is connect with cylinder body bottom, the other end and air blast
Machine connects.
Ignition tip is equipped in the gas pipeline.
Description of the drawings
Fig. 1 faces internal structure schematic diagram for a kind of heat accumulating type tar disposition burner of the utility model embodiment.
Fig. 2 is the overlooking structure diagram that a kind of heat accumulating type tar of the utility model embodiment disposes burner.
Fig. 3 is the structural schematic diagram of catalytic thermal storage ball in the utility model embodiment.
Specific implementation mode
A kind of embodiment of the utility model is described in detail in conjunction with Fig. 1, Fig. 2, Fig. 3.
The present embodiment is to solve the above problems by the following technical programs:A kind of heat accumulating type tar disposition burner
Including:Cylinder 2, catalytic thermal storage ball 3, catalysis net 4, gas pipeline 5, catalytic thermal storage ball 3 is using SiO2 as matrix, outside
Reticular structure 9 is wrapped up in portion, and catalysis net 4 is located at inner barrel, 4 top of catalysis net and 5 lower part phase of gas pipeline with gas pipeline 5
Even, gas pipeline 5 is connected through 2 top of cylinder with 2 external world of cylinder, and 4 lower part of catalysis net is connected through cylinder 2 with 2 external world of cylinder,
Reticular structure 9 is that same coke tar cracking is catalyzed material composition with catalysis net 4.
2 side top of cylinder is equipped with air inlet 1.
Inner barrel is embedded with refractory brick, on the one hand reinforces cylinder, and still further aspect prevents long term high temperature operation from being made to cylinder
At damage, package thermal insulation material prevents energy leakage, inside from cannot keep high temperature outside cylinder.
2 bottom of cylinder is equipped with admission line 7, and 7 one end of the admission line is connect with 2 bottom of cylinder, the other end and air blast
Machine 8 connects.
The fuel gas of tar is carried by being ignited when ignition device, generates heat, catalytic thermal storage bead passes through
After accumulation of heat, cylinder body temperature is maintained at 800 ~ 900 DEG C, and at this temperature, the combustible gas for carrying tar enters cylinder elder generation and urges
Change regenertive small ball contact, catalytic thermal storage bead is with SiO2It, being capable of catalytic tar cracking as the tar composite catalyst of matrix
For fuel gas, the reticular structure of nickel-base material is enclosed on catalytic thermal storage bead, catalysis net equally uses nickel-base material, Ni-based
Material also can effectively accelerate coke tar cracking as tar catalyst, and the combustible gas for carrying tar from top to bottom, is first stored with catalysis
Hot bead comes into full contact with, and enters back into the catalysis net of lower section, and tar is all cracked into fuel gas, enters combustion by catalysis net
Feed channel mixes under the action of admission line and air blower with outside air, is discharged after being lighted by electric ignition device.
The utility model proposes a kind of heat accumulating type tar to dispose burner, and simple in structure, deft design can efficiently use
Calory burning removes the tar mixed in fuel gas.
Claims (5)
1. a kind of heat accumulating type tar disposes burner, it is characterised in that:Including cylinder, catalytic thermal storage ball, catalysis net, Gas Pipe
Reticular structure is wrapped up in road, the catalytic thermal storage ball outside, and the catalysis net is located at inner barrel, catalysis net top with gas pipeline
It is connected with gas pipeline lower part, gas pipeline is connected through cylinder top with the cylinder external world, and cylinder is run through in the catalysis net lower part
It is connected with the cylinder external world, the reticular structure is that same coke tar cracking is catalyzed material composition, the catalytic thermal storage ball with catalysis net
It is constituted with coke tar cracking catalysis material.
2. a kind of heat accumulating type tar according to claim 1 disposes burner, it is characterised in that:The cylinder side top
Equipped with air inlet.
3. a kind of heat accumulating type tar according to claim 1 disposes burner, it is characterised in that:The inner barrel is embedded with
Thermal insulation material is wrapped up in refractory brick, cylinder outside.
4. a kind of heat accumulating type tar according to claim 1 disposes burner, it is characterised in that:The cylinder body bottom is equipped with
Admission line, described admission line one end are connect with cylinder body bottom, and the other end is connect with air blower.
5. a kind of heat accumulating type tar according to claim 1 disposes burner, it is characterised in that:It is set in the gas pipeline
There is ignition tip.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721790978.8U CN207661804U (en) | 2017-12-20 | 2017-12-20 | A kind of heat accumulating type tar disposition burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721790978.8U CN207661804U (en) | 2017-12-20 | 2017-12-20 | A kind of heat accumulating type tar disposition burner |
Publications (1)
Publication Number | Publication Date |
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CN207661804U true CN207661804U (en) | 2018-07-27 |
Family
ID=62941923
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201721790978.8U Expired - Fee Related CN207661804U (en) | 2017-12-20 | 2017-12-20 | A kind of heat accumulating type tar disposition burner |
Country Status (1)
Country | Link |
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CN (1) | CN207661804U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107906543A (en) * | 2017-12-20 | 2018-04-13 | 安徽省升泰节能科技服务有限公司 | A kind of heat accumulating type tar disposes burner |
-
2017
- 2017-12-20 CN CN201721790978.8U patent/CN207661804U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107906543A (en) * | 2017-12-20 | 2018-04-13 | 安徽省升泰节能科技服务有限公司 | A kind of heat accumulating type tar disposes burner |
CN107906543B (en) * | 2017-12-20 | 2024-04-12 | 南京硬核科技服务有限公司 | Tar disposal burner |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180727 Termination date: 20181220 |
|
CF01 | Termination of patent right due to non-payment of annual fee |