CN107312570A - Biomass gasifying furnace - Google Patents

Biomass gasifying furnace Download PDF

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Publication number
CN107312570A
CN107312570A CN201710672782.7A CN201710672782A CN107312570A CN 107312570 A CN107312570 A CN 107312570A CN 201710672782 A CN201710672782 A CN 201710672782A CN 107312570 A CN107312570 A CN 107312570A
Authority
CN
China
Prior art keywords
furnace body
biomass gasifying
transverse slat
deflector
furnace
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.)
Withdrawn
Application number
CN201710672782.7A
Other languages
Chinese (zh)
Inventor
龙志威
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 CN201710672782.7A priority Critical patent/CN107312570A/en
Publication of CN107312570A publication Critical patent/CN107312570A/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J1/00Production of fuel gases by carburetting air or other gases without pyrolysis
    • C10J1/20Carburetting gases other than air
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/58Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
    • C10J3/60Processes
    • C10J3/64Processes with decomposition of the distillation products
    • C10J3/66Processes with decomposition of the distillation products by introducing them into the gasification zone
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/09Mechanical details of gasifiers not otherwise provided for, e.g. sealing means
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/0916Biomass
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0973Water
    • C10J2300/0976Water as steam
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0983Additives

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid-Fuel Combustion (AREA)

Abstract

The invention discloses a kind of biomass gasifying furnace, belong in gas-fired equipment technical field, the biomass gasifying furnace, including furnace body, the furnace body has heated oxide area, reducing zone and fuel area in preparation successively from the bottom up;Corresponding in the furnace body of the reducing zone by deflector be provided with U-shaped reduction passage;The furnace body peripheral protective corresponding to the heated oxide area has water vapour to occur room;The venthole that room occurs for the water vapour is connected with the entrance of the reduction passage;At least two risers that the deflector includes transverse slat and stood on side by side on the transverse slat;The deflector has the transverse slat to be oppositely arranged, the riser is staggered two;The present invention can solve existing biomass gasifying furnace and exist that the recovery time is shorter, the problem of reduction reaction is not exclusively and the heat that produces of zoneofoxidation is lost in because of radiation.

Description

Biomass gasifying furnace
Technical field
The present invention relates to gas-fired equipment technical field, especially a kind of biomass gasifying furnace.
Background technology
Biomass gasifying furnace is that one kind makes biomass be heated in zoneofoxidation, occurs oxidation reaction generation carbon dioxide, and Carbon dioxide is occurred reduction reaction in reducing zone and carbon and water vapour and produce the imflammable gas such as carbon monoxide, methane, hydrogen Molecule after, then through fuel area in preparation carry out Pintsch process, drying, the equipment to obtain preferable firepower;Due to it safely, defend Raw, environmental protection, and biomass material is by agricultural crop straw, forest tree castoff, edible fungi residues, cattle and sheep animal manure and all flammable things Matter is made, and is a kind of inexhaustible regenerated resources, therefore be widely applied;But existing biogas Change stove and exist that the recovery time is shorter, the problem of reduction reaction is not exclusively and the heat that produces of zoneofoxidation is lost in because of radiation.
The content of the invention
The present invention provides a kind of biomass gasifying furnace, and the biomass gasifying furnace can solve existing biomass gasifying furnace and deposit Shorter in the recovery time, reduction reaction is not exclusively and the heat that produces of zoneofoxidation because of radiation the problem of be lost in.
In order to solve the above problems, the technical solution adopted in the present invention is:This biomass gasifying furnace, including stove sheet There are heated oxide area, reducing zone and fuel area in preparation in body, the furnace body successively from the bottom up;Corresponding to the reducing zone U-shaped reduction passage is provided with by deflector in the furnace body;Corresponding to the furnace body periphery in the heated oxide area Shield has water vapour to occur room;The venthole that room occurs for the water vapour is connected with the entrance of the reduction passage.
In above-mentioned technical proposal, more specifically technical scheme can also be:The deflector includes transverse slat and stood side by side In at least two risers on the transverse slat;The deflector has the transverse slat to be oppositely arranged, two that the riser is staggered It is individual.
Further:Provided with the fire grate for conveying and carrying biomass in the heated oxide area, the institute below the fire grate Furnace body is stated provided with combustion adjuvant entrance.
Further:Exported corresponding to combustible gas is offered on the furnace body of the fuel area in preparation.
By adopting the above-described technical solution, the present invention has the advantages that compared with prior art:
1st, due to being provided with U-shaped reduction passage by deflector in the furnace body corresponding to reducing zone;Corresponding to heated oxide area The furnace body peripheral protective have water vapour occur room;Water vapour occurs the venthole of room and is connected with reducing the entrance of passage; So, carbon dioxide is occurred reduction reaction with carbon and water vapour in U-shaped reduction passage, extend its reaction time, no But their reduction reactions are ensure that fully and completely, moreover, the thermal energy that heated oxide area gives off, can make water vapour occur room Interior boiling water directly produces water vapour, has saved the energy;
2nd, at least two risers for transverse slat being included due to deflector and being stood on side by side on transverse slat;Deflector has the transverse slat relative Set, be staggered two of riser;So, on the premise of complete reduction reaction being met ensureing the length for reducing passage, Structure is simpler;
3rd, because the furnace body below fire grate is provided with combustion adjuvant entrance;Biomass combustion can be made more complete.
Brief description of the drawings
Fig. 1 is the structural representation of the embodiment of the present invention.
Embodiment
Embodiment one
The invention will be further described for embodiment below in conjunction with the accompanying drawings:
There is heated oxide area III in biomass gasifying furnace shown in Fig. 1, including furnace body 1, furnace body 1 successively from the bottom up, go back Former area II and fuel area in preparation I;Corresponding to deflector 2 is provided with the furnace body 1 of reducing zone II, deflector is by transverse slat 21 and side by side Two risers 22 stood on transverse slat 21 are constituted;Deflector has two, and the transverse slats 21 of two deflectors is oppositely arranged, riser 22 is handed over Mistake sets the U-shaped reduction passage constituted in reducing zone II;There is water vapour corresponding to the peripheral protective of furnace body 1 in heated oxide area III Generation room IV;Water vapour occurs room IV and is provided with the I of the water inlet IV and O of venthole IV, and the O of venthole IV of room IV occurs for water vapour with going back The I of entrance II of former passage is connected;The O of outlet II of reduction passage is connected with the I of entrance I of fuel area in preparation I, corresponding to fuel Combustible gas is offered on the furnace body 1 of area in preparation I and exports I O, combustible gas exports I O and is connected with the entrance of gas-cooker;Heat oxygen Change provided with the fire grate 3 for conveying and carrying biomass in area III, the furnace body 1 of the lower section of fire grate 3 is provided with the I of combustion adjuvant entrance III;Plus The carbon dioxide gas in thermal oxide area III exports III O and is connected with reducing the I of entrance II of passage.During work, heated oxide area III gives birth to Into carbon dioxide occur reduction reaction with carbon and water vapour in U-shaped reduction passage, extend its reaction time, not only protect Their reduction reactions are demonstrate,proved fully and completely, moreover, the thermal energy that heated oxide area gives off, can make water vapour occur indoor Boiling water directly produces water vapour, has saved the energy.
Embodiment two
Deflector is made up of transverse slat 21 and four risers 22 stood on side by side on transverse slat 21;Remaining is identical with embodiment one.

Claims (4)

1. there are heated oxide area, reducing zone successively from the bottom up in a kind of biomass gasifying furnace, including furnace body, the furnace body With fuel area in preparation;It is characterized in that:Corresponding in the furnace body of the reducing zone by deflector be provided with U-shaped reduction Passage;The furnace body peripheral protective corresponding to the heated oxide area has water vapour to occur room;Room occurs for the water vapour Venthole is connected with the entrance of the reduction passage.
2. biomass gasifying furnace according to claim 1, it is characterised in that:The deflector includes transverse slat and stood side by side In at least two risers on the transverse slat;The deflector has the transverse slat to be oppositely arranged, two that the riser is staggered It is individual.
3. biomass gasifying furnace according to claim 1 or 2, it is characterised in that:Provided with conveying in the heated oxide area And the furnace body below the fire grate of biomass, the fire grate is carried provided with combustion adjuvant entrance.
4. biomass gasifying furnace according to claim 3, it is characterised in that:Corresponding on the housing of the fuel area in preparation Offer combustible gas outlet.
CN201710672782.7A 2017-08-08 2017-08-08 Biomass gasifying furnace Withdrawn CN107312570A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710672782.7A CN107312570A (en) 2017-08-08 2017-08-08 Biomass gasifying furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710672782.7A CN107312570A (en) 2017-08-08 2017-08-08 Biomass gasifying furnace

Publications (1)

Publication Number Publication Date
CN107312570A true CN107312570A (en) 2017-11-03

Family

ID=60175518

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710672782.7A Withdrawn CN107312570A (en) 2017-08-08 2017-08-08 Biomass gasifying furnace

Country Status (1)

Country Link
CN (1) CN107312570A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110041966A (en) * 2019-03-15 2019-07-23 福州鑫裕协新能源有限公司 A kind of biomass gasifying furnace

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6232185A (en) * 1985-08-02 1987-02-12 Babcock Hitachi Kk Coal gasification oven
CN2916408Y (en) * 2006-04-11 2007-06-27 海盐大明环保节能科技有限公司 Biomass gasification furnace
US20100028818A1 (en) * 2008-08-01 2010-02-04 Zhongcheng Huang Process and apparatus for burning coal instead of oil
CN201908074U (en) * 2010-11-23 2011-07-27 杭州佑农生物科技有限公司 Downdraft gasification system
CN102252320A (en) * 2011-06-25 2011-11-23 山东百川同创能源有限公司 Biomass low-nitrogen direct combustion boiler
CN104087342A (en) * 2014-07-31 2014-10-08 邱云原 Biomass gasification furnace capable of decoking by utilizing furnace body sandwich structure

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6232185A (en) * 1985-08-02 1987-02-12 Babcock Hitachi Kk Coal gasification oven
CN2916408Y (en) * 2006-04-11 2007-06-27 海盐大明环保节能科技有限公司 Biomass gasification furnace
US20100028818A1 (en) * 2008-08-01 2010-02-04 Zhongcheng Huang Process and apparatus for burning coal instead of oil
CN201908074U (en) * 2010-11-23 2011-07-27 杭州佑农生物科技有限公司 Downdraft gasification system
CN102252320A (en) * 2011-06-25 2011-11-23 山东百川同创能源有限公司 Biomass low-nitrogen direct combustion boiler
CN104087342A (en) * 2014-07-31 2014-10-08 邱云原 Biomass gasification furnace capable of decoking by utilizing furnace body sandwich structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110041966A (en) * 2019-03-15 2019-07-23 福州鑫裕协新能源有限公司 A kind of biomass gasifying furnace

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Application publication date: 20171103

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