CN106010653B - Biomass gasifying furnace - Google Patents

Biomass gasifying furnace Download PDF

Info

Publication number
CN106010653B
CN106010653B CN201610518414.2A CN201610518414A CN106010653B CN 106010653 B CN106010653 B CN 106010653B CN 201610518414 A CN201610518414 A CN 201610518414A CN 106010653 B CN106010653 B CN 106010653B
Authority
CN
China
Prior art keywords
air inlet
inlet pipe
combustion chamber
vaporizer
nozzle
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.)
Expired - Fee Related
Application number
CN201610518414.2A
Other languages
Chinese (zh)
Other versions
CN106010653A (en
Inventor
温洲
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.)
Henan Electric Research New Energy Technology Co ltd
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 CN201610518414.2A priority Critical patent/CN106010653B/en
Publication of CN106010653A publication Critical patent/CN106010653A/en
Application granted granted Critical
Publication of CN106010653B publication Critical patent/CN106010653B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • 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
    • C10J3/72Other features
    • C10J3/82Gas withdrawal means
    • C10J3/84Gas withdrawal means with means for removing dust or tar from the gas
    • 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
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1603Integration of gasification processes with another plant or parts within the plant with gas treatment
    • C10J2300/1606Combustion processes

Landscapes

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

Abstract

The invention discloses a kind of biomass gasifying furnaces, comprising: the furnace body being vertically arranged comprising vaporizer, combustion chamber and collection chamber, combustion chamber are arranged in the lower section of vaporizer, communicate with vaporizer, and the top of vaporizer is arranged in collection chamber, communicate with vaporizer;Second pyrolysis room, is circumferentially positioned at the outside of combustion chamber, and tar cracking catalyst is filled in second pyrolysis room;Multiple air inlet pipe, tangential direction of the one end of air inlet pipe along combustion chamber stretches to combustion chamber, the other end of air inlet pipe is connected to the combustion-supporting gas feedway being arranged in outside furnace body, and multiple air inlet pipe are uniformly arranged relative to combustion chamber, the nozzle of air inlet pipe is flat mouth shape, and the length direction of the nozzle of air inlet pipe is axial parallel with combustion chamber, the width of nozzle is 0.3~0.5cm;The outside of furnace body is arranged in gas-guide tube, and one end is connected to collection chamber, and the other end is connected to second pyrolysis room.Present invention reduces the tar contents of fuel gas, improve the quality of fuel gas.

Description

Biomass gasifying furnace
Technical field
The present invention relates to a kind of biomass gasifying furnaces.
Background technique
Biomass includes plant, excrement and the town and country debirs of nature, is a kind of non-fossil renewable energy.With The energy utilization patterns that biomass is directly burnt are compared, and have extended use, reduction carrying out utilizing after biomass pyrogenation gasification The advantages of pollution, clean and effective.But China's biomass pyrogenation gasification technology falls behind relatively, biomass pyrogenation gasification is handled at present Equipment mainly uses fixed-bed gasification furnace and the normal pressure fluidized bed gasification furnace, and wherein fixed-bed gasification furnace in production process due to that can produce Raw a large amount of phenol water, tar content is high, and secondary pollution is more serious, and single furnace gas production is small, and the flammable gas calorific value of output is low, is limited It uses;The in-furnace temperature fluctuation range of the normal pressure fluidized bed gasification furnace is big, and controlling of production process is difficult, and operational reliability is poor, heat waste Consumption is big, and deslagging carbon content is high, and more containing nitrogen amount in the fuel gas produced, calorific value is low, and combustion gas dust content height purifies difficulty etc. Deficiency, therefore fail to be used widely so far.Also, due to containing tar, life after biomass combustion in the lignin of biology At fuel gas in tar content it is also higher, cause the fuel gas generated to have a peculiar smell, when use pollutes environment, also unfavorable In conveying and storage.The backwardness of biomass pyrogenation gasification technology, the clean and effective for hindering China's biomass energy utilize.
Summary of the invention
The present invention has designed and developed a kind of biomass gasifying furnace that can lower tar content in fuel gas.
Technical solution provided by the invention are as follows:
A kind of biomass gasifying furnace, comprising:
The furnace body being vertically arranged comprising vaporizer, combustion chamber and collection chamber, the combustion chamber are arranged in the vaporizer Lower section, communicated with the vaporizer, the top of the vaporizer is arranged in the collection chamber, communicates with the vaporizer;
Second pyrolysis room, is circumferentially positioned at the outside of the combustion chamber, and the second pyrolysis room is filled coke tar cracking and urged Agent;
One end of multiple air inlet pipe, the air inlet pipe stretches in the combustion chamber along the tangential direction of the combustion chamber Portion, the other end of the air inlet pipe is connected to the combustion-supporting gas feedway being arranged in outside furnace body, and multiple air inlet pipe are opposite Be uniformly arranged in the combustion chamber, the nozzle of the air inlet pipe is flat mouth shape, and the length direction of the nozzle of the air inlet pipe with The axial direction of the combustion chamber is parallel, and the width of the nozzle is 0.3~0.5cm;
The outside of the furnace body is arranged in gas-guide tube, and one end is connected to the collection chamber, and other end connection is described secondary Cracking room.
Preferably, in the biomass gasifying furnace, the tar cracking catalyst is lime stone and magnesium carbonate.
Preferably, in the biomass gasifying furnace, the multiple air inlet pipe is distributed along the axial direction of the combustion chamber At multilayer, every layer of air inlet pipe includes several air inlet pipe, adjacent two layers air inlet pipe 2~3cm of interval.
Biomass gasifying furnace of the present invention provides a second pyrolysis room, and second pyrolysis room is circumferentially positioned at burning The outside of room is provided with multiple air inlet pipe in the combustion chamber, and one end of air inlet pipe is protruded into along the tangential direction of combustion chamber To combustion chamber, and the nozzle of air inlet pipe is flat mouth shape, and the width design of nozzle is 0.3~0.5cm, thus in combustion chamber Inner wall near temperature be significantly higher than combustion chamber, send out the tar in fuel gas more fully in second pyrolysis room Raw second pyrolysis reaction.Present invention reduces the tar contents of fuel gas, improve the quality of fuel gas.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of biomass gasifying furnace of the present invention.
Specific embodiment
Present invention will be described in further detail below with reference to the accompanying drawings, to enable those skilled in the art referring to specification text Word can be implemented accordingly.
As shown in Figure 1, the present invention provides a kind of biomass gasifying furnace, comprising: the furnace body 1 being vertically arranged comprising gasification The lower section of the vaporizer is arranged in room 8, combustion chamber 3 and collection chamber 2, the combustion chamber 3, communicates with the vaporizer, described The top of the vaporizer is arranged in collection chamber, communicates with the vaporizer;Second pyrolysis room is circumferentially positioned at the burning Tar cracking catalyst is filled in the outside of room 3, the second pyrolysis room 5;Multiple air inlet pipe 6, one end of the air inlet pipe is along institute The tangential direction for stating combustion chamber stretches to the combustion chamber, and the other end of the air inlet pipe, which is connected to, to be arranged outside furnace body Combustion-supporting gas feedway, and multiple air inlet pipe are uniformly arranged relative to the combustion chamber, and the nozzle 7 of the air inlet pipe is flat Mouthful shape, and the length direction of the nozzle of the air inlet pipe is axial parallel with the combustion chamber, the width of the nozzle for 0.3~ 0.5cm;The outside of the furnace body is arranged in gas-guide tube 4, and one end is connected to the collection chamber, and other end connection is described secondary Cracking room.
In the present invention, fuel gas containing tar enters collection chamber, and is entered in second pyrolysis room by gas-guide tube.Two secondary fissures Solution room is circumferentially positioned at the outside of combustion chamber, inside fills tar cracking catalyst.Fuel gas containing tar is in second pyrolysis room It is interior, by the heating for the indoor heat that burns, second pyrolysis reaction occurs under the catalytic action of tar cracking catalyst, thus Reduce tar content.
Especially for the indoor heat of burning is made full use of, the present invention is provided with multiple air inlet pipe, one end of air inlet pipe Be stretched to along the tangential direction of combustion chamber burning it is indoor, the other end of air inlet pipe, which is communicated to, is arranged in helping outside furnace body On combustion gas body feeding, in this way, air inlet pipe will supply combustion-supporting gas to combustion chamber along tangential direction.And due to air inlet pipe Caliber very little, only 0.3~0.5cm, can combustion chamber inner wall formed a combustion-supporting gas air film.Due to depositing for air film , the combustion case near the inner wall of combustion chamber can be more preferable, and more sufficiently, and then keep the temperature near the inner wall of combustion chamber higher, To keep the indoor temperature of second pyrolysis also higher, the indoor fuel gas containing tar of second pyrolysis is promoted sufficiently to react.
In order to promote the inside in combustion chamber to form uniform combustion-supporting gas air film, the nozzle of air inlet pipe is designed to flat mouth Shape, and the width design of nozzle is 0.3~0.5cm.Uniform combustion-supporting gas air film can guarantee near wall in the combustion chamber More evenly, i.e., the temperature near Inner Wall of Combustion Chamber also more evenly, and then guarantees the indoor second pyrolysis reaction of second pyrolysis for burning Also uniformly occur.
The present invention takes full advantage of existing heat source, improves the utilization efficiency to the energy.
Preferably, in the biomass gasifying furnace, the tar cracking catalyst is lime stone and magnesium carbonate.At this In embodiment, burning room temperature can choose 800~1000 DEG C.
Preferably, in the biomass gasifying furnace, the multiple air inlet pipe is distributed along the axial direction of the combustion chamber At multilayer, every layer of air inlet pipe includes several air inlet pipe, adjacent two layers air inlet pipe 2~3cm of interval.The embodiment is more conducive to Near Inner Wall of Combustion Chamber formed combustion-supporting gas uniform air film, improve the uniformity of air film, thus make in the combustion chamber wall it is attached Close burning also more evenly, and then makes the more uniform temperature near Inner Wall of Combustion Chamber, and the indoor heating temperature of second pyrolysis is also more Uniformly.
The tar removal efficiency of excellent present invention fuel gas containing tar can achieve 99.99%.
Although the embodiments of the present invention have been disclosed as above, but its is not only in the description and the implementation listed With it can be fully applied to various fields suitable for the present invention, for those skilled in the art, can be easily Realize other modification, therefore without departing from the general concept defined in the claims and the equivalent scope, the present invention is simultaneously unlimited In specific details and legend shown and described herein.

Claims (3)

1. a kind of biomass gasifying furnace, comprising:
The furnace body being vertically arranged comprising vaporizer, combustion chamber and collection chamber, the combustion chamber are arranged under the vaporizer Side, communicates, the top of the vaporizer is arranged in the collection chamber, communicates with the vaporizer with the vaporizer;
Second pyrolysis room is circumferentially positioned at the outside of the combustion chamber;
The outside of the furnace body is arranged in gas-guide tube, and one end is connected to the collection chamber, and the other end is connected to the second pyrolysis Room;
It is characterized by further comprising:
Fill tar cracking catalyst in the second pyrolysis room;
Multiple air inlet pipe, tangential direction of the one end of the air inlet pipe along the combustion chamber stretch to the combustion chamber, institute The other end for stating air inlet pipe is connected to the combustion-supporting gas feedway being arranged in outside furnace body, and multiple air inlet pipe are relative to described Combustion chamber is uniformly arranged, and the nozzle of the air inlet pipe is flat mouth shape, and the length direction of the nozzle of the air inlet pipe and the combustion The axial parallel of room is burnt, the width of the nozzle is 0.3 ~ 0.5cm.
2. biomass gasifying furnace as described in claim 1, which is characterized in that the tar cracking catalyst is lime stone and carbon Sour magnesium.
3. biomass gasifying furnace as described in claim 1, which is characterized in that the multiple air inlet pipe is along the combustion chamber It axially is scattered in multilayer, every layer of air inlet pipe includes several air inlet pipe, adjacent two layers air inlet pipe 2 ~ 3cm of interval.
CN201610518414.2A 2016-06-29 2016-06-29 Biomass gasifying furnace Expired - Fee Related CN106010653B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610518414.2A CN106010653B (en) 2016-06-29 2016-06-29 Biomass gasifying furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610518414.2A CN106010653B (en) 2016-06-29 2016-06-29 Biomass gasifying furnace

Publications (2)

Publication Number Publication Date
CN106010653A CN106010653A (en) 2016-10-12
CN106010653B true CN106010653B (en) 2019-01-04

Family

ID=57106985

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610518414.2A Expired - Fee Related CN106010653B (en) 2016-06-29 2016-06-29 Biomass gasifying furnace

Country Status (1)

Country Link
CN (1) CN106010653B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110041966B (en) * 2019-03-15 2024-06-21 福州鑫裕协新能源有限公司 Biomass gasification stove

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201507956U (en) * 2009-08-06 2010-06-16 昆明电研新能源科技开发有限公司 Household biomass gasifier
CN101781579A (en) * 2010-04-07 2010-07-21 王治刚 Biomass gasification method and biomass gasification furnace
CN103196137A (en) * 2012-01-04 2013-07-10 刘柏谦 Multi-burner pulverized coal combustion device
JP2015059159A (en) * 2013-09-18 2015-03-30 株式会社Ihi Apparatus for reforming tar in gasified-gas
CN104791848A (en) * 2014-11-25 2015-07-22 西北工业大学 Combustion chamber flame cylinder wall face with blade grid channel multi-inclined-hole cooling manner adopted
CN205279155U (en) * 2015-10-10 2016-06-01 上海交通大学 Ran shao shi cui puts out pore structure

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201507956U (en) * 2009-08-06 2010-06-16 昆明电研新能源科技开发有限公司 Household biomass gasifier
CN101781579A (en) * 2010-04-07 2010-07-21 王治刚 Biomass gasification method and biomass gasification furnace
CN103196137A (en) * 2012-01-04 2013-07-10 刘柏谦 Multi-burner pulverized coal combustion device
JP2015059159A (en) * 2013-09-18 2015-03-30 株式会社Ihi Apparatus for reforming tar in gasified-gas
CN104791848A (en) * 2014-11-25 2015-07-22 西北工业大学 Combustion chamber flame cylinder wall face with blade grid channel multi-inclined-hole cooling manner adopted
CN205279155U (en) * 2015-10-10 2016-06-01 上海交通大学 Ran shao shi cui puts out pore structure

Also Published As

Publication number Publication date
CN106010653A (en) 2016-10-12

Similar Documents

Publication Publication Date Title
CN105333439B (en) Secondary high-temperature gasification incineration system for garbage
CN107760387B (en) High-nitrogen biomass waste gasification combustion heat supply system and process
CN105588127B (en) Using the boiler combustion system of biomass gasification device
CN102776007A (en) Continuous biomass pyrolytic carbon gas-oil poly-generation system
CN101850967B (en) Integrated device and method for preparing activated carbon by using organic wastes
CN105273763A (en) Heat pipe heating type biomass and coal segmented collaborative pyrolysis system
CN101328423A (en) Method and apparatus for removing superadiabatic partial oxidation coke tar and coke and gas reform
CN106010653B (en) Biomass gasifying furnace
CN102443445B (en) Process and device for continuously gasifying biomass and simultaneously removing tar in moving bed
CN102226106A (en) Biomass vapourizing furnace
CN105733685B (en) Biomass gasifying furnace
CN202214340U (en) Continuous gasification and tar removing device for biomass moving bed
CN106118757B (en) Biomass gasifying furnace with equipment of supplying gas
CN101538484B (en) Internal combustion heating rotation conical biomass gasification furnace
CN204593396U (en) A kind of refuse disposal installation
CN104595903B (en) A kind of biomass garbage pyrolysis incineration device
CN106118745B (en) The biomass gasifying furnace of cleavable tar
CN115869877A (en) Solar energy coupled biomass energy heat and hydrogen co-production system and method
CN203079920U (en) Spiral tar cracking gasifier
CN105969426B (en) Biomass gasifying furnace with cracking room
CN210945516U (en) Updraft type pyrolysis gasification system
CN210945494U (en) Anaerobic middle-temperature downdraft type pyrolysis device
CN104099119B (en) Biomass fluidization pyrolysis liquefaction device
CN202047041U (en) Biomass gasification furnace
CN202229394U (en) Energy-saving emission-reducing fire tube boiler with stock bin

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20181109

Address after: 315012 room 1025, Liyuan North Road, Haishu District, Ningbo, Zhejiang, China, 755

Applicant after: Jin Qi

Address before: 536000 the Guangxi Zhuang Autonomous Region Beihai Yinhai District North Sichuan Road Tian Bi garden 12 stories 08 rooms.

Applicant before: Wen Zhou

GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20190911

Address after: 450000 Jinshui District, Zhengzhou City, Henan Province, Building No. 1, No. 68, Jingsan Road, 15th floor, 1502

Patentee after: Henan Electric Research New Energy Technology Co.,Ltd.

Address before: 315012 Zhejiang Province, Ningbo city Haishu District Liyuan Road No. 755 room 1025

Patentee before: Jin Qi

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190104