CN103727537A - Oxygen-enriched combustion device for waste thermal decomposition combustible gas - Google Patents

Oxygen-enriched combustion device for waste thermal decomposition combustible gas Download PDF

Info

Publication number
CN103727537A
CN103727537A CN201210388914.0A CN201210388914A CN103727537A CN 103727537 A CN103727537 A CN 103727537A CN 201210388914 A CN201210388914 A CN 201210388914A CN 103727537 A CN103727537 A CN 103727537A
Authority
CN
China
Prior art keywords
oxygen
pipeline
gas
refuse pyrolysis
air
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
Application number
CN201210388914.0A
Other languages
Chinese (zh)
Inventor
黄广禧
李高奇
周锐海
陈明忠
吴桂香
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201210388914.0A priority Critical patent/CN103727537A/en
Publication of CN103727537A publication Critical patent/CN103727537A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

The invention discloses an oxygen-enriched combustion device for waste thermal decomposition combustible gas and relates to a combustion device, in particular to an oxygen-enriched combustion device for combustible gas generated from thermal decomposition of waste in the treatment process. The oxygen-enriched combustion device for the waste thermal decomposition combustible gas comprises an oxygen pipeline, a waste thermal decomposition gas pipeline, an air pipeline, a gas mixing pipeline, a combustor, a distributor, steel pipes and an air blower. The waste thermal decomposition gas pipeline is connected with the gas mixing pipeline, the air pipeline is connected with the gas mixing pipeline, the oxygen pipeline is connected with the gas mixing pipeline, the outlet of the air blower is connected with the inlet of the air pipeline, the outlet of the gas mixing pipeline is connected with the combustor, the combustor is composed of the distributor and the steel pipes, the distributor is connected with the multiple steel pipes, and the mixed gas is evenly distributed to all the steel pipes by the distributor. Because the oxygen-enriched combustion technology is adopted for the oxygen-enriched combustion device, the oxygen content of the mixed gas is increased, the gas combustion quality is improved, emission of harmful constituents is reduced, and the oxygen-enriched combustion device is favorable for environmental protection.

Description

The oxygen-enriched burning device of refuse pyrolysis combustible gas
 
Technical field
The oxygen-enriched burning device of refuse pyrolysis combustible gas of the present invention relates to a kind of burner, the oxygen-enriched burning device of the combustible gas that particularly a kind of disposal of refuse pyrolysis produces.
Background technology
In refuse pyrolysis process, produce a large amount of fuel gas, because the gas component that refuse pyrolysis produces is comparatively complicated, adopt the method for directly burning to fail effectively to make combustion gas fully burn, cause combustion efficiency poor, the thermal efficiency of fuel is low, not burned toxic gas is followed flue gas and is discharged together, causes the loss of heat and the pollution of environment.
Oxygen-enriched combustion technology refers to that in combustion gas, oxygen content replaces the one efficient overheavy firing technology of air as combustion-supporting gas higher than 21% oxygen-enriched air.Oxygen-enriched combusting reaction speed is fast, and flame temperature is high, can effectively improve the thermal efficiency of combustion gas, reduces hear rate, reaches the object of effective energy-saving and emission-reduction, reduces the pollution to environment.Due to the gas component complexity that refuse pyrolysis produces, adopt directly burning to there will be the tail gas impurity content after burning high, as carbon monoxide, charcoal particle etc.For addressing this problem, adopt oxygen-enriched combustion technology to carry out the combustion gas that combustion refuse pyrolysis produces, thereby improve the burning velocity of combustion gas, improve burning quality, be conducive to the protection of environment.
Summary of the invention
Object of the present invention is for overcoming the deficiencies in the prior art, the combustible gas that provides a kind of disposal of refuse pyrolysis to produce, improve the burning velocity of combustion gas, improve burning quality, the oxygen-enriched burning device of the refuse pyrolysis combustible gas that the combustible gas that refuse pyrolysis is produced burns under excess oxygen.
For achieving the above object, the oxygen-enriched burning device of refuse pyrolysis combustible gas of the present invention comprises oxygen channel, refuse pyrolysis gas pipeline, air duct, combustion gas mixing pipeline, burner, distributor, steel pipe, air-blaster, refuse pyrolysis gas pipeline is connected with combustion gas mixing pipeline, air duct is connected with combustion gas mixing pipeline, oxygen channel is connected with combustion gas mixing pipeline, the outlet of air-blaster is connected with air duct entrance, combustion gas mixing pipe outlet is connected with burner, burner is comprised of distributor and steel pipe, distributor connects many steel pipes, distributor is uniformly distributed air mixture to every steel pipe.
Refuse pyrolysis gas pipeline of the present invention is enclosed within oxygen channel outside while installing, combustion gas mixing pipeline is enclosed within outside refuse pyrolysis gas pipeline; Oxygen channel passes refuse pyrolysis gas pipeline and combustion gas mixing pipeline as innermost layer.
Refuse pyrolysis gas pipeline outlet of the present invention is provided with adjusting control valve.
Between the outlet of air-blaster of the present invention and air duct entrance, be provided with adjusting control valve.
Oxygen channel outlet of the present invention is provided with adjusting control valve.
Combustion gas mixing pipe outlet of the present invention can be connected with multiple burners simultaneously.
The present invention can, by regulating the control valve in oxygen channel, refuse pyrolysis gas pipeline, air duct, control various air inflows, makes the oxygen content of air mixture 30% ~ 35%.
Beneficial effect of the present invention: the combustible gas complicated component that refuse pyrolysis produces, adopt the mode of directly burning can not reach clean-burning effect, be difficult to the harmful components burning in combustion gas.The present invention adopts oxygen-enriched combustion technology, and the combustion gas that refuse pyrolysis is produced mixes with a certain amount of oxygen, air, improves the content of oxygen in air mixture; thereby improve the burn rate of combustible gas; improve the burning quality of combustion gas, reduce the discharge of harmful components, be conducive to the protection of environment.
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present invention.
Accompanying drawing 2 is burner structure schematic diagrames of the present invention.
The specific embodiment
Below in conjunction with accompanying drawing, the invention will be further described.
In figure: oxygen channel 1, refuse pyrolysis gas pipeline 2, air duct 3, combustion gas mixing pipeline 4, burner 5, distributor 6, steel pipe 7, air-blaster 8.
As accompanying drawing 1, shown in accompanying drawing 2, the oxygen-enriched burning device of refuse pyrolysis combustible gas of the present invention comprises oxygen channel 1, refuse pyrolysis gas pipeline 2, air duct 3, combustion gas mixing pipeline 4, burner 5, distributor 6, steel pipe 7, air-blaster 8, refuse pyrolysis gas pipeline 2 is connected with combustion gas mixing pipeline 4, air duct 3 is connected with combustion gas mixing pipeline 4, oxygen channel 1 is connected with combustion gas mixing pipeline 4, the outlet of air-blaster 8 is connected with air duct 3 entrances, 4 outlets of combustion gas mixing pipeline are connected with burner 5, burner 5 is comprised of distributor 6 and steel pipe 7, distributor 6 connects many steel pipes 7, distributor 6 is uniformly distributed air mixture to every steel pipe 7.Refuse pyrolysis gas pipeline 2 is enclosed within oxygen channel 1 outside, and air duct 3 is connected with combustion gas mixing pipeline 4, and combustion gas mixing pipeline 4 is enclosed within outside refuse pyrolysis gas pipeline 2; Oxygen channel 1 passes refuse pyrolysis gas pipeline 2 and combustion gas mixing pipeline 4 as innermost layer; 2 outlets of refuse pyrolysis gas pipeline are provided with adjusting control valve; The outlet of air-blaster 8 is connected with air duct 3 entrances, between the outlet of air-blaster 8 and air duct 3 entrances, is provided with adjusting control valve.
Burner 5 is comprised of distributor 6 and steel pipe 7, and distributor 6 connects many steel pipes 7, and distributor 6 is uniformly distributed air mixture to every steel pipe 7.
4 outlets of combustion gas mixing pipeline can be communicated with multiple burners 5 simultaneously.
Regulate the control valve in oxygen channel 1, refuse pyrolysis gas pipeline 2, air duct 3, control the air inflow of oxygen, air, refuse pyrolysis combustion gas, make the oxygen content of air mixture 30% ~ 35%, air mixture is pooled in combustion gas mixing pipeline 4.4 outlets of combustion gas mixing pipeline are connected with burner 5, and air mixture is fully burned in burner 5, is conducive to improve the burn rate of combustible gas, improves burning quality, is conducive to the protection of environment simultaneously.

Claims (6)

1. the oxygen-enriched burning device of a refuse pyrolysis combustible gas, it is characterized in that comprising oxygen channel, refuse pyrolysis gas pipeline, air duct, combustion gas mixing pipeline, burner, distributor, steel pipe, air-blaster, refuse pyrolysis gas pipeline is connected with combustion gas mixing pipeline, air duct is connected with combustion gas mixing pipeline, oxygen channel is connected with combustion gas mixing pipeline, the outlet of air-blaster is connected with air duct entrance, combustion gas mixing pipe outlet is connected with burner, burner is comprised of distributor and steel pipe, distributor connects many steel pipes, distributor is uniformly distributed air mixture to every steel pipe.
2. the oxygen-enriched burning device of refuse pyrolysis combustible gas according to claim 1, it is characterized in that refuse pyrolysis gas pipeline is enclosed within oxygen channel outside, combustion gas mixing pipeline is enclosed within outside refuse pyrolysis gas pipeline, and oxygen channel is through refuse pyrolysis gas pipeline and combustion gas mixing pipeline.
3. the oxygen-enriched burning device of refuse pyrolysis combustible gas according to claim 1, is characterized in that the outlet of refuse pyrolysis gas pipeline is provided with adjusting control valve.
4. the oxygen-enriched burning device of refuse pyrolysis combustible gas according to claim 1, is characterized in that being provided with adjusting control valve between the outlet of air-blaster and air duct entrance.
5. the oxygen-enriched burning device of refuse pyrolysis combustible gas according to claim 1, is characterized in that oxygen channel outlet is provided with adjusting control valve.
6. the oxygen-enriched burning device of refuse pyrolysis combustible gas according to claim 1, is characterized in that combustion gas mixing pipe outlet is connected with multiple burners.
CN201210388914.0A 2012-10-15 2012-10-15 Oxygen-enriched combustion device for waste thermal decomposition combustible gas Pending CN103727537A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210388914.0A CN103727537A (en) 2012-10-15 2012-10-15 Oxygen-enriched combustion device for waste thermal decomposition combustible gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210388914.0A CN103727537A (en) 2012-10-15 2012-10-15 Oxygen-enriched combustion device for waste thermal decomposition combustible gas

Publications (1)

Publication Number Publication Date
CN103727537A true CN103727537A (en) 2014-04-16

Family

ID=50451736

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210388914.0A Pending CN103727537A (en) 2012-10-15 2012-10-15 Oxygen-enriched combustion device for waste thermal decomposition combustible gas

Country Status (1)

Country Link
CN (1) CN103727537A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109237494A (en) * 2018-09-20 2019-01-18 方政 A kind of environment-protection low-consumption burner
CN110701612A (en) * 2019-10-14 2020-01-17 中冶南方都市环保工程技术股份有限公司 Combustion ratio optimization control device and system

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4969814A (en) * 1989-05-08 1990-11-13 Union Carbide Corporation Multiple oxidant jet combustion method and apparatus
CN2549329Y (en) * 2002-03-14 2003-05-07 戴德 Jet oxygen-enriched combustor
CN1850370A (en) * 2006-05-15 2006-10-25 滕清华 Life-garbage comprehensive treatment technology
CN102607035A (en) * 2012-03-30 2012-07-25 杭州恒明环保技术有限公司 Process of municipal solid waste treatment and utilization system
CN202868681U (en) * 2012-10-15 2013-04-10 黄广禧 Oxygen-enriched combustion device for waste pyrolysis flammable gas

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4969814A (en) * 1989-05-08 1990-11-13 Union Carbide Corporation Multiple oxidant jet combustion method and apparatus
CN2549329Y (en) * 2002-03-14 2003-05-07 戴德 Jet oxygen-enriched combustor
CN1850370A (en) * 2006-05-15 2006-10-25 滕清华 Life-garbage comprehensive treatment technology
CN102607035A (en) * 2012-03-30 2012-07-25 杭州恒明环保技术有限公司 Process of municipal solid waste treatment and utilization system
CN202868681U (en) * 2012-10-15 2013-04-10 黄广禧 Oxygen-enriched combustion device for waste pyrolysis flammable gas

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109237494A (en) * 2018-09-20 2019-01-18 方政 A kind of environment-protection low-consumption burner
CN109237494B (en) * 2018-09-20 2020-11-13 马鞍山市润启新材料科技有限公司 Environment-friendly low-consumption combustion device
CN110701612A (en) * 2019-10-14 2020-01-17 中冶南方都市环保工程技术股份有限公司 Combustion ratio optimization control device and system

Similar Documents

Publication Publication Date Title
CN105351942B (en) A kind of pyrolytic gasification waste incinerator using oxygen-enriched combustion technology
CN203190418U (en) Novel garbage pyrolysis incineration equipment
CN104696949A (en) Two-stage process denitrification method of coal fired boiler
CN204420998U (en) A kind of low NOx combustion apparatus from preheating and coal dust sectional combustion
CN105674257A (en) Two-stage-adjustable steam plasma swirl burner
CN202868681U (en) Oxygen-enriched combustion device for waste pyrolysis flammable gas
CN205402704U (en) Two -stage adjustable steam plasma cyclone burner
CN103727537A (en) Oxygen-enriched combustion device for waste thermal decomposition combustible gas
CN101713538A (en) Combustion method of low-pressure and low-concentration methane gas and device
CN107860011B (en) Carbon black tail gas incineration boiler with carbon black drying waste gas treatment function
CN102798129B (en) Efficient thermal oxidation furnace for low afterburning-amount smoke constant-speed grading reaction
CN202546785U (en) Low-heating value tail gas combustion engine
CN204478025U (en) Fire coal boiler fume two-phase method denitrification apparatus
CN201539862U (en) Combustion device of a low pressure low concentration methane gas
CN2830902Y (en) Full premixed burner of gas water heater
CN103438456B (en) Biomass gas burner
CN202521630U (en) Air supply system of biomass particle burner
CN110841478A (en) Flue gas treatment device utilizing circulating flue gas
CN202420214U (en) Waste-heat utilization flue after-burning device
CN207797009U (en) A kind of fire coal coupled biological matter burning air-cone
CN202328181U (en) Flue gas circulation backfiring device
CN204962838U (en) Boiler oxygen boosting burning gas supply system
CN202329103U (en) Low-carbon energy-saving gas heat treatment tunnel furnace
CN203147752U (en) System for blending combustion of low-calorific value gas in circulating fluidized bed boiler
CN202813398U (en) Low complementary combustion volume flue gas constant-speed fractional reaction efficient thermal oxidation furnace

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20140416