CN101294707A - Biomass fuel thermal decomposition vaporization combustion method and apparatus - Google Patents

Biomass fuel thermal decomposition vaporization combustion method and apparatus Download PDF

Info

Publication number
CN101294707A
CN101294707A CNA2007100721772A CN200710072177A CN101294707A CN 101294707 A CN101294707 A CN 101294707A CN A2007100721772 A CNA2007100721772 A CN A2007100721772A CN 200710072177 A CN200710072177 A CN 200710072177A CN 101294707 A CN101294707 A CN 101294707A
Authority
CN
China
Prior art keywords
fuel
pyrogenation
pyrolysis
storehouse
spiral propeller
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.)
Granted
Application number
CNA2007100721772A
Other languages
Chinese (zh)
Other versions
CN101294707B (en
Inventor
韩枫
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 CN2007100721772A priority Critical patent/CN101294707B/en
Publication of CN101294707A publication Critical patent/CN101294707A/en
Application granted granted Critical
Publication of CN101294707B publication Critical patent/CN101294707B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Solid-Fuel Combustion (AREA)

Abstract

A pyrogenation gasification combustion device for biomass fuel is characterized in that a pyrogenation device is added inside a hearth of a boiler and is composed of a pyrogenation cylinder and a pyrogenation grate, and a material feeding device is arranged outside the hearth. The biomass fuel is pushed forward by a main spiral propeller and is gradually compressed when passing through a fuel passage to improve the degree of compaction and prevent pyrogenation gas from escaping; the biomass fuel is pushed to move on by subsequent fuel after entering the pyrogenation cylinder, and gradually falls on the pyrogenation grate to contact oxygen for ignition; the pyrogenation cylinder is heated by flame after ignition; the biomass fuel in the pyrogenation cylinder is heated to a temperature higher than that of pyrogenation; the biomass fuel carries out gas-solid separation; the gas can only escape from the flame on the pyrogenation grate; the combustible component therein is subjected to forced ignition; the flame goes up to the upper part of the hearth along the lateral face of the pyrogenation cylinder and is burnt out; at the same time the pyrogenation cylinder is heated for the continuous pyrogenation reaction therein; and the solid on the pyrogenation grate is broken to pieces, and falls or continuously burns on the pyrogenation grate.

Description

Biomass fuel thermal decomposition vaporization combustion method and device
Technical field
The present invention relates to a kind of biomass fuel thermal decomposition vaporization combustion technology, especially a kind of biomass fuel thermal decomposition vaporization combustion method and device.
Background technology
Because the coal resources worsening shortages, countries in the world all utilize technology at postgraduate's substance combustion, and to solve the problem that energy crisis was produced, at present, the boiler of the biological substance for combustion of having released all is to research and develop on the technical foundation of coal-burning boiler.But,, adopt the coal-burning boiler technology to be difficult to form stable burning condition because biomass fuel moisture content is big, volatilization point is low, fugitive constituent is many, energy density is low.So feasible method is with living beings vaporization or charing, improves energy density, sends in the boiler and burns.But all there is system complex in the variety of way that produces at present, and investment is big, and problems such as inefficiency can't substitute the coal-burning boiler that generally uses.
Summary of the invention
The purpose of this invention is to provide a kind of biomass fuel thermal decomposition gasified combustion apparatus, this device utilizes the heat energy of premature combustion fuel in the burner hearth of boiler, with follow-up fuel after pyrolysis under the condition of anaerobic, combine with oxygen again the burning, this device can overcome the deficiencies in the prior art, makes burning utilize the heat energy of living beings convenient and feasible.
The method of the thermal decomposition gasification combustion of biomass fuel is: when the biomass fuel quality conforms with designing requirement, opening main fuel storehouse spiral propeller advances biomass fuel, increase through fuel channel and enter the pyrolysis tube after the tight ness rating of fuel and drop on the pyrolysis fire grate and lighted a fire, igniting back flame heat pyrolysis tube and pyrolysis fire grate, biomass fuel in the pyrolysis tube is heated up, surpass pyrolysis temperature gradually, gas solid separation, gas is got angry by the pyrolysis fire grate and is overflowed in the flame, be forced to igniting, flame rises to the upper furnace after-flame along pyrolysis tube side, give the heating of pyrolysis tube simultaneously, make its inner pyrolytic reaction continue to carry out, drop on the combustion grate after solid carbon on the pyrolysis fire grate is cataclasm and burn away, when the biomass fuel quality does not conform with designing requirement, open auxiliary fuel storehouse spiral propeller earlier, main fuel storehouse spiral propeller is opened in the back, at this moment the high-quality coal in the auxiliary fuel storehouse, fall into the main fuel storehouse spiral propeller of bottom, main fuel storehouse earlier, biomass fuel in coal in the auxiliary fuel storehouse and the main fuel storehouse mixes propelling in the spiral propeller of main fuel storehouse, its pyrolysis, gasification, combustion method is with last identical, method for the thermal decomposition gasification combustion of realizing biomass fuel, the present invention is the inside at the burner hearth of the boiler of prior art, increased pyrolysis installation, pyrolysis installation is by the pyrolysis tube, the pyrolysis fire grate is formed, the pyrolysis tube adopts exotic material, its cross section is for falling " U " font, latter half of is following for sealing, following and the front of its first half is the opening shape, the pyrolysis fire grate is arranged in its lower section, there is feeding device the outside of burner hearth, feeding device is by the main fuel storehouse, main fuel storehouse spiral propeller, auxiliary fuel storehouse and auxiliary fuel storehouse spiral propeller are formed, main fuel storehouse spiral propeller is arranged at bottom, main fuel storehouse, its import communicates with bottom, main fuel storehouse, there is fuel channel the front of main fuel storehouse spiral propeller, shrink gradually in the interior cross section of fuel channel, the fuel channel small end is connected with ring flange with the pyrolysis tube, its big end is connected with ring flange with the outlet of main fuel storehouse spiral propeller, spiral propeller is arranged at bottom, auxiliary fuel storehouse, and the outlet of auxiliary fuel storehouse spiral propeller is between main fuel storehouse and spiral propeller junction surface, main fuel storehouse.
The present invention than its beneficial effect is compared with prior art:
1. fuel is applied widely, does not need meticulous reorganizing and outfit, can also be under the situation that biomass fuel does not continue, and using easily, the coal of deposit is fuel.
2. gas burns required secondary wind by entering above the combustion grate, and by solid burning article, resistance is not little, has reduced the airborne dust effect.
3. pyrolysis gas can only overflow from the carbon fire, and fresh air and stable incendiary source are arranged on the direction of advance, thereby guarantees that combustible component is wherein ignited and smooth combustion.
4. thermal decomposition vaporization device and burner hearth do not have the structural relation of mutual restriction, can be according to user's different specific requirement, design the boiler of different performance (steam or hot water, have and press or normal pressure), different size, and also can transform existing boiler.
Description of drawings
The present invention is further described below in conjunction with accompanying drawing
Fig. 1 is the fundamental diagram of biomass fuel thermal decomposition vaporization combustion method of the present invention and device;
Fig. 2 is A-A, the B-B cutaway view of Fig. 1
1. main fuel storehouses among the figure, 2. auxiliary fuel storehouse, 3. burner hearth, 4. pyrolysis tube, 5. combustion grate, 6. pyrolysis fire grate, 7. fuel channel, 8. main fuel storehouse spiral propeller, 9. auxiliary fuel storehouse spiral propeller
The specific embodiment
The method of the thermal decomposition gasification combustion of biomass fuel is: when the biomass fuel quality conforms with designing requirement, opening main fuel storehouse spiral propeller 8 advances biomass fuel, increase through fuel channel 7 and enter pyrolysis tube 4 after the tight ness rating of fuel and drop on the pyrolysis fire grate 6 and lighted a fire, igniting back flame heat pyrolysis tube 4 and pyrolysis fire grate 6, biomass fuel in the pyrolysis tube is heated up, surpass pyrolysis temperature gradually, gas solid separation, gas is got angry by the pyrolysis fire grate and is overflowed in the flame, be forced to igniting, flame rises to the upper furnace after-flame along pyrolysis tube side, give the heating of pyrolysis tube simultaneously, make its inner pyrolytic reaction continue to carry out, drop on the combustion grate after solid carbon on the pyrolysis fire grate is cataclasm and burn away, when the biomass fuel quality does not conform with designing requirement, open auxiliary fuel storehouse spiral propeller 9 earlier, main fuel storehouse spiral propeller is opened in the back, at this moment the high-quality coal in the auxiliary fuel storehouse, fall into the main fuel storehouse spiral propeller of bottom, main fuel storehouse earlier, biomass fuel in coal in the auxiliary fuel storehouse and the main fuel storehouse mixes propelling in the spiral propeller of main fuel storehouse, its pyrolysis, gasification, combustion method is with last identical, pyrolysis installation is by the pyrolysis tube, the pyrolysis fire grate is formed, the pyrolysis tube adopts exotic material, its cross section is for falling " U " font, seal below the first half, its latter half of following and back is the opening shape, the pyrolysis fire grate is arranged in its lower section, there is feeding device the outside of burner hearth, feeding device is by the main fuel storehouse, main fuel storehouse spiral propeller, auxiliary fuel storehouse and auxiliary fuel storehouse spiral propeller are formed, main fuel storehouse spiral propeller is arranged at bottom, main fuel storehouse, its import communicates with bottom, main fuel storehouse, there is fuel channel the front of main fuel storehouse spiral propeller, shrink gradually in the interior cross section of fuel channel, and small end is connected with ring flange with the pyrolysis tube, big end is connected with ring flange with the outlet of main fuel storehouse spiral propeller, spiral propeller is arranged at bottom, auxiliary fuel storehouse, and the outlet of auxiliary fuel storehouse spiral propeller is between main fuel storehouse and spiral propeller junction surface, main fuel storehouse.
The operation principle of biomass fuel thermal decomposition vaporization combustion method and device is: dress biomass fuel in the main fuel storehouse 1, auxiliary fuel storehouse 2 high-grade fuel such as coaling, when if the biomass fuel quality in the main fuel storehouse does not conform with designing requirement, open auxiliary fuel storehouse spiral propeller 9, high-grade fuels such as coal in a part of auxiliary fuel storehouse are pushed earlier in the main fuel storehouse spiral propeller 8, other parts are replenished by the main fuel in main fuel storehouse, change two conveyer rotating speeds, can adjust the proportioning of two kinds of fuel, two kinds of fuel are mixed propelling in the spiral propeller of main fuel storehouse, make quality conform with designing requirement, thereby guarantee the stable of burning and continue to carry out into the fuel combination of stove.When if the biomass fuel quality in the main fuel storehouse conforms with designing requirement, inactive auxiliary fuel storehouse spiral propeller, use main fuel fully, when main fuel " is gone hungry ", also can burn auxilliary fuel fully, biomass fuel is promoted to advance by main fuel storehouse spiral propeller, by fuel channel 7 time, gradually reduced, improve packing, play the effect of sealed door, stop pyrolysis gas to be overflowed thus, after entering pyrolysis tube 4, return to fluffy state, moving in the environment in anaerobic under the promotion of follow-up fuel, drop on gradually on the pyrolysis fire grate 6 to contact and lighted a fire with oxygen, igniting back flame heat pyrolysis tube 4 and pyrolysis fire grate 6, biomass fuel in the pyrolysis tube is heated up, surpass pyrolysis temperature gradually, the biomass fuel gas solid separation, gas can only be overflowed from the pyrolysis fire grate is got angry flame, and combustible component wherein is forced to igniting, flame rises to burner hearth 3 top after-flames along pyrolysis tube side, give the heating of pyrolysis tube simultaneously, make its inner pyrolytic reaction continue to carry out, drop to or pushed away to fall on the combustion grate 5 burning away after the solid on the pyrolysis fire grate is cataclasm to after-flame by follow-up fuel.

Claims (2)

1, a kind of biomass fuel thermal decomposition vaporization combustion method and device, it is characterized in that: the method for the thermal decomposition gasification combustion of biomass fuel is: when the biomass fuel quality conforms with designing requirement, opening main fuel storehouse spiral propeller advances biomass fuel, increase through fuel channel and enter the pyrolysis tube after the tight ness rating of fuel and drop on the pyrolysis fire grate and lighted a fire, igniting back flame heat pyrolysis tube and pyrolysis fire grate, biomass fuel in the pyrolysis tube is heated up, surpass pyrolysis temperature gradually, gas solid separation, gas is got angry by the pyrolysis fire grate and is got out in the flame, be forced to igniting, flame rises to the upper furnace after-flame along pyrolysis tube side, give the heating of pyrolysis tube simultaneously, make its inner pyrolytic reaction continue to carry out, drop on the combustion grate after solid carbon on the pyrolysis fire grate is cataclasm and burn away, when the biomass fuel quality does not conform with designing requirement, open auxiliary fuel storehouse spiral propeller earlier, main fuel storehouse spiral propeller is opened in the back, at this moment the high-quality coal in the auxiliary fuel storehouse, fall into the main fuel storehouse spiral propeller of bottom, main fuel storehouse earlier, biomass fuel in coal in the auxiliary fuel storehouse and the main fuel storehouse mixes propelling in the spiral propeller of main fuel storehouse, its pyrolysis, gasification, combustion method is with last identical.
2, a kind of biomass fuel thermal decomposition vaporization combustion method according to claim 1 and device, its feature also is: pyrolysis installation is by the pyrolysis tube, the pyrolysis fire grate is formed, the pyrolysis tube adopts exotic material, its cross section is for falling " U " font, first half following for sealing, its latter half of following and back is the opening shape, the pyrolysis fire grate is arranged in its lower section, there is feeding device the outside of burner hearth, feeding device is by the main fuel storehouse, main fuel storehouse spiral propeller, auxiliary fuel storehouse and auxiliary fuel storehouse spiral propeller are formed, main fuel storehouse spiral propeller is arranged at bottom, main fuel storehouse, its import communicates with bottom, main fuel storehouse, there is fuel channel the front of main fuel storehouse spiral propeller, the fuel channel small end is connected with ring flange with the pyrolysis tube, its big end is connected with ring flange with the outlet of main fuel storehouse spiral propeller, and spiral propeller is arranged at bottom, auxiliary fuel storehouse, and the outlet of auxiliary fuel storehouse spiral propeller is between main fuel storehouse and spiral propeller junction surface, main fuel storehouse.
CN2007100721772A 2007-04-27 2007-04-27 Biomass fuel thermal decomposition vaporization combustion method Expired - Fee Related CN101294707B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2007100721772A CN101294707B (en) 2007-04-27 2007-04-27 Biomass fuel thermal decomposition vaporization combustion method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2007100721772A CN101294707B (en) 2007-04-27 2007-04-27 Biomass fuel thermal decomposition vaporization combustion method

Publications (2)

Publication Number Publication Date
CN101294707A true CN101294707A (en) 2008-10-29
CN101294707B CN101294707B (en) 2011-09-14

Family

ID=40065146

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2007100721772A Expired - Fee Related CN101294707B (en) 2007-04-27 2007-04-27 Biomass fuel thermal decomposition vaporization combustion method

Country Status (1)

Country Link
CN (1) CN101294707B (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101706098B (en) * 2009-12-02 2011-05-11 孔繁利 Biomass burner
CN102278204A (en) * 2010-06-11 2011-12-14 郭聪贤 Powdery solid fuel combustion and work application method and device
CN102287844A (en) * 2011-06-10 2011-12-21 内蒙古绿茵生物能源科技有限公司包头研发中心 Feeding device of multi-ash-content biomass granule fuel combustor
WO2011160299A1 (en) * 2010-06-23 2011-12-29 Che Zhanbin Method for combusting solid fuel, burner and combustion device
CN102748754A (en) * 2012-07-25 2012-10-24 章丘市宇龙机械有限公司 Biomass boiler
CN102767838A (en) * 2012-07-19 2012-11-07 江苏太湖锅炉股份有限公司 Feeding device of biomass and coal co-firing boiler
CN102803851A (en) * 2009-06-16 2012-11-28 拉斯·约翰森 Method and device for continuously operating pyrolysis reactor
CN102809161A (en) * 2012-08-28 2012-12-05 上海博士高环保设备工程有限公司 Safe waste material feeding device suitable for incinerator
CN103175206A (en) * 2011-12-26 2013-06-26 福州耕耘专利开发有限公司 Sunlight-accumulating garbage incineration device
CN103471126A (en) * 2013-08-30 2013-12-25 江苏太湖锅炉股份有限公司 Double-fuel feeding device
CN103471125A (en) * 2013-08-30 2013-12-25 江苏太湖锅炉股份有限公司 Double-feeding boiler system for coal briquettes and other solid fuels
CN103759250A (en) * 2014-01-24 2014-04-30 韩枫 Boiler by adoption of pyrolysis vaporization combustion method
WO2015058409A1 (en) * 2013-10-25 2015-04-30 车战斌 Solid fuel combustion method and combustor
CN104807016A (en) * 2015-05-23 2015-07-29 梁长安 Environment-friendly and high-efficient garbage cracking furnace
CN107883380A (en) * 2017-11-09 2018-04-06 北京恒信卓元科技有限公司 Gasification and melting refuse disposal installation and its process
CN108251160A (en) * 2018-02-07 2018-07-06 宜昌市汇宜兴新能源科技有限公司 A kind of high conversion biomass gasification equipment
CN112664979A (en) * 2020-12-28 2021-04-16 华北电力大学 Cooking range

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2073546U (en) * 1990-07-05 1991-03-20 中国科学院工程热物理研究所 Gasification combusting stoves using biological fuels
CN2401549Y (en) * 1999-11-30 2000-10-18 山东工业大学热能与环保工程技术研究中心 Stalk two-stage gasifying device
GB0305224D0 (en) * 2003-03-07 2003-04-09 Hudol Ltd Gasification apparatus and method
CN1690516A (en) * 2004-04-24 2005-11-02 韩枫 Pyrogenic decomposition type boiler for combustion of refuse and purifying installation thereof
CN1814699A (en) * 2005-02-05 2006-08-09 韩枫 Boiler capable of producing jointly oil, gas and carbon and heat-energy by pyrolyzing biological fuels
UA77108C2 (en) * 2005-03-28 2006-10-16 Anatolii Tymofiiovych Neklesa Method for thermal processing of domestic waste and unit for its implementation
CN1272404C (en) * 2005-06-16 2006-08-30 山东省科学院能源研究所 Low-tar biomass gasifying method and apparatus
CN2893450Y (en) * 2006-03-09 2007-04-25 大连蓝天干燥设备有限公司 Evaporization combustion furnace

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102803851A (en) * 2009-06-16 2012-11-28 拉斯·约翰森 Method and device for continuously operating pyrolysis reactor
CN101706098B (en) * 2009-12-02 2011-05-11 孔繁利 Biomass burner
CN102278204A (en) * 2010-06-11 2011-12-14 郭聪贤 Powdery solid fuel combustion and work application method and device
WO2011160299A1 (en) * 2010-06-23 2011-12-29 Che Zhanbin Method for combusting solid fuel, burner and combustion device
CN102985755A (en) * 2010-06-23 2013-03-20 车战斌 Method for combusting solid fuel, burner and combustion device
CN102985755B (en) * 2010-06-23 2015-07-22 车战斌 Solid fuel burner and combustion device
CN102287844B (en) * 2011-06-10 2013-07-24 内蒙古绿茵生物能源科技有限公司包头研发中心 Feeding device of multi-ash-content biomass granule fuel combustor
CN102287844A (en) * 2011-06-10 2011-12-21 内蒙古绿茵生物能源科技有限公司包头研发中心 Feeding device of multi-ash-content biomass granule fuel combustor
CN103175206B (en) * 2011-12-26 2015-05-27 福州耕耘专利开发有限公司 Sunlight-accumulating garbage incineration device
CN103175206A (en) * 2011-12-26 2013-06-26 福州耕耘专利开发有限公司 Sunlight-accumulating garbage incineration device
CN102767838A (en) * 2012-07-19 2012-11-07 江苏太湖锅炉股份有限公司 Feeding device of biomass and coal co-firing boiler
CN102767838B (en) * 2012-07-19 2015-10-14 江苏太湖锅炉股份有限公司 Living beings, coal for mixing combustion boiler feeding device
CN102748754A (en) * 2012-07-25 2012-10-24 章丘市宇龙机械有限公司 Biomass boiler
CN102809161A (en) * 2012-08-28 2012-12-05 上海博士高环保设备工程有限公司 Safe waste material feeding device suitable for incinerator
CN102809161B (en) * 2012-08-28 2014-08-20 上海博士高环保设备工程有限公司 Safe waste material feeding device suitable for incinerator
CN103471125A (en) * 2013-08-30 2013-12-25 江苏太湖锅炉股份有限公司 Double-feeding boiler system for coal briquettes and other solid fuels
CN103471126A (en) * 2013-08-30 2013-12-25 江苏太湖锅炉股份有限公司 Double-fuel feeding device
CN103471125B (en) * 2013-08-30 2017-12-01 江苏太湖锅炉股份有限公司 The double feeding systems of boiler of coal cinder and other solid fuels
WO2015058409A1 (en) * 2013-10-25 2015-04-30 车战斌 Solid fuel combustion method and combustor
CN103759250A (en) * 2014-01-24 2014-04-30 韩枫 Boiler by adoption of pyrolysis vaporization combustion method
CN103759250B (en) * 2014-01-24 2015-12-09 韩枫 Use the boiler of thermal decomposition vaporization combustion method
CN104807016A (en) * 2015-05-23 2015-07-29 梁长安 Environment-friendly and high-efficient garbage cracking furnace
CN107883380A (en) * 2017-11-09 2018-04-06 北京恒信卓元科技有限公司 Gasification and melting refuse disposal installation and its process
CN108251160A (en) * 2018-02-07 2018-07-06 宜昌市汇宜兴新能源科技有限公司 A kind of high conversion biomass gasification equipment
CN112664979A (en) * 2020-12-28 2021-04-16 华北电力大学 Cooking range

Also Published As

Publication number Publication date
CN101294707B (en) 2011-09-14

Similar Documents

Publication Publication Date Title
CN101294707B (en) Biomass fuel thermal decomposition vaporization combustion method
CN104748125B (en) Pyrolysis volatile matter combustion system
CN105423306A (en) Double-layer mechanical grate type waste gasifying incinerator and processing method thereof
CN104534454B (en) Air heating furnace of biomass particle forming fuels
CN105062565A (en) Biomass fixed bed oxygen-rich gasification furnace
CN204786347U (en) Biomass gasification phase separating combustion furnace
CN114806614B (en) Rotary kiln pyrolysis carbonization device and process based on smoke injection recycling
CN103499108A (en) Biomass energy-saving furnace
CN207849374U (en) A kind of vertical more fire grate garbage pyrogenation incinerators
CN201680417U (en) Biomass energy-saving environment-protection cooking-heating furnace
CN206176390U (en) Domestic waste pyrolysis gasification treatment system
CN201795475U (en) Boiler burning biomass solid-formed fuels
CN103615712A (en) Large-sized biomass gasification furnace burner
CN2380569Y (en) Low-suction type organism-gasifying furnace
CN201330237Y (en) Biomass direct-combustion gasification furnace
CN203273948U (en) Biomass energy-saving furnace
CN110345633A (en) A kind of biomass gasification system and method that can provide domestic hot-water and have both heating function
CN201262412Y (en) Biomass semi-gasification domestic boiler
CN105465792A (en) Circulating air supply system of mechanical fire gate type waste gasification incinerator
EP2246411A1 (en) Method and apparatus for producing combustible gas with biomass
CN203571714U (en) Large-scale biomass gasifier burner
CN201014728Y (en) Horizontal atmospheric fire tube hot water boiler dedicated for biomass fuel direct combustion
CN207999849U (en) Biomass energy-saving furnace
CN102607016B (en) Boiler thermodynamic system and process by utilizing biomass particles as fuel and technology
CN201310924Y (en) Gas-making compound combustion vertical-type 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
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110914

Termination date: 20160427