CN1810928A - Comprehensive biomass solidifying, carbonizing and gasifying utilization process - Google Patents

Comprehensive biomass solidifying, carbonizing and gasifying utilization process Download PDF

Info

Publication number
CN1810928A
CN1810928A CNA2006100459785A CN200610045978A CN1810928A CN 1810928 A CN1810928 A CN 1810928A CN A2006100459785 A CNA2006100459785 A CN A2006100459785A CN 200610045978 A CN200610045978 A CN 200610045978A CN 1810928 A CN1810928 A CN 1810928A
Authority
CN
China
Prior art keywords
biomass
raw material
carbonizing
gasifying
solidifying
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
CNA2006100459785A
Other languages
Chinese (zh)
Inventor
李峰耀
李依唐
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 CNA2006100459785A priority Critical patent/CN1810928A/en
Publication of CN1810928A publication Critical patent/CN1810928A/en
Pending legal-status Critical Current

Links

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
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Abstract

The comprehensive biomass solidifying, carbonizing and gasifying utilization process in reproducible energy source includes the following steps: collecting biomass material wood dust, forest leftover, etc.; stoving and separating in a separator; carbonizing and extruding to product charcoal; reducing and cracking to separate mixed inflammable gas, and eliminating tar to obtain biomass fuel gas. The present invention can utilize biomass comprehensively and improve environment.

Description

A kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process
Technical field: the present invention relates to the renewable energy source domain, is a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process of raw material with biomass wood chip, stalk etc. in the renewable energy source development and use particularly.
Background technology: at present, energy scarcity, the underground fossil class energy is fewer and feweri, has formed worldwide energy dilemma.Look for another way, exploitation is renewable energy source on the ground, just becomes human very urgent task.Exploitation such as renewable energy sources such as biomass energy, wind energy, sun power is risen in countries in the world.For this reason, the Chinese government issued " People's Republic of China's renewable energy source method " on January 1st, 2006, with legal form protection and the development of support renewable energy source.Adopt agricultural crop straw or forestry waste to do the biomass energy exploitation of raw material, presented the fine impetus in China.As biomass power generation, biomass (stalk) shaped fuel, biological fuel gas, biomass charcoal, biomass methyl alcohol, ethanol or the like.But its complete processing and preparation method all adopt the method for single development and use biomass energy, have both wasted limited Energy resources on the ground, continuous again contaminate environment.Ward off as, single processing biological (stalk) shaped fuel, the cost height, expense is big, can't transfer investor's enthusiasm.Ward off as, single employing earth kiln formula method processing biological charcoal, the production cycle is long, and expense is big, and 1 kilogram of charcoal of every production, promptly discharges 1-2 cube of obnoxious flavour, and contaminate environment now has been subjected to environmental administration's restriction.Single processing biological combustion gas just produces a large amount of breezes, nowhere digestion.Moreover, build the gas station investment greatly, it is little to produce effects, and the few people of enterprise make inquiries.Annual government drops into villages and small towns, substantial contribution supply rural area, builds public welfare biological fuel gas station, makes every effort to promote this technology, produces little effect.Comprehensive biomass solidifying, carbonizing and gasifying utilization process is one of effective ways that fully develop in geodyte mass-energy source.Therefore develop a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process is new problem anxious to be solved both at home and abroad always.
The purpose of this invention is to provide a kind of being skillfully constructed, versatility, scientific and reasonable, creativity consciousness is arranged, easy to use, reduce expenses, cheap, improved the comprehensive utilization ratio of biomass renewable energy sources, changed and processed the necessary discharging waste gas of charcoal, contaminate environment in the past, the processing biological combustion gas, the phenomenon that waste residue discharges nowhere has and has both saved biomass energy, has improved a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process of the social benefit and the performance of enterprises again.
Summary of the invention: the object of the present invention is achieved like this: its preparation technology is: at first the collection of biological raw material is a sawdust, wood shavings, branch, the wooden class raw material of trunk forestry waste, be processed into the 0.5-15mm powder through pulverizer, deposit in the feed bin standby, drying machine material loading winch is sent in the drying machine raw material dry, it is thermal source that drying oven adopts biological fuel gas, the byproduct that produces during the used comprehensive biomass solidifying, carbonizing and gasifying utilization process processing of its drying oven charcoal, it is biological fuel gas, raw material in the drying machine is behind drying and dewatering under 60 ℃ of-100 ℃ of temperature, under the induced draft fan effect, separate through separator, separator upper end vapour discharge and moisture, the lower end spills dried raw material, the preparation method of charing is with the wooden class raw material of sawdust after its first moulding, after biomass forming machine squeezes out bar-like raw material, in the biomass carbonated gasification combustion furnace of packing into, under the temperature control effect, process high temperature high-quality machine-made charcoal and biological fuel gas; The preparation method of its first charing aftershaping packs wooden material powder in the biomass carbonated gasification combustion furnace into, generates black solid powdered carbon and biological fuel gas under the temperature control effect, and it is machine-made charcoal that powdered carbon is squeezed into carbon rod through biomass forming machine; Biomass material can be maize straw, rice husk, faggot, corn cob, oil crops cot agricultural crop straw; The raw material water content does not surpass 12% can be dry; The material powder can be wooden material powder 50%, straw material powder 50%; Elder generation's charing aftershaping is the tackiness agent that the powdered carbon after the charing processing is inserted 0.5%-5%, stir evenly, be squeezed into Φ 30 * 150mm through spiral biomass charcoal powder shaper, the hollow carbon rod of Φ 50 * 450mm specification, it is the common machine-made charcoal of low temperature, the rated pressure of carbon rod extrusion molding is 15mpa, and density is at 0.7-0.9g/mc 3Between, calorific value reaches that 6500-7000 kilocalorie/kilogram, carbon content reach 70%-75%, ash content reaches 6%-8%, is packaged into product; Charing is with the wooden class raw material of dried sawdust after elder generation's moulding, be squeezed into Φ 30 * 150mm through hydraulic biomass fuel forming machine or spiral biological substance fuel forming machine, the hollow bar-shaped raw material for standby of Φ 50 * 450mm specification, the rated pressure of bar extrusion molding is 15-31mpa, and density is at 0.8-1.2g/mc 3Between; Machine-shaping is biomass molding fuel without the bar of charing; Elder generation's charing aftershaping is that the raw material powder after the preparation is quantitative by 300-1000kg, the igniting back banking in the biomass carbonated gasification combustion furnace of packing into, the material powder is under anoxic condition spontaneous combustion 48-50 hour in the stove, produces water vapour and non-combustible gas when temperature in the stove reaches 150 ℃-300 ℃, in time discharges by discharge outlet, when temperature in the stove reaches 300 ℃-700 ℃, biomass are through reduction, cracking and polyreaction, and inflammable gas is isolated in the generate energy conversion, be biological fuel gas, recyclable; It is quantitative that the bar-like raw material of extrusion molding is pressed 500-2000kg, the igniting banking in back in the biomass carbonated gasification combustion furnace of packing into, produce water vapour and non-combustible gas when temperature reaches 150 ℃-430 ℃ in the bar under anoxic condition spontaneous combustion 48-50 hour, stove, in time discharge by discharge outlet; When temperature reached 430 ℃-900 ℃ in the stove, biomass were through reduction, cracking and polyreaction, and inflammable gas is isolated in the generate energy conversion, is biological fuel gas, and is recyclable; Bar through high-temperature calcination is the stronger high temperature high-quality machine-made charcoal of rigidity; Its calorific value reaches that 7500-8500 kilocalorie/kilogram, carbon content reach 80%-85%, ash content reaches 5-6%, is packaged into product; Biomass carbonated gasification combustion furnace endogenous substance is in the anoxycausis process, when reaching 150 ℃-430 ℃, temperature produces water vapour and non-combustible gas, in time discharge by discharge outlet, when temperature reaches 430 ℃-900 ℃, biomass begin reduction, cracking and polyreaction, the generate energy conversion, progressively separate, formation matter is hard, the black solid charcoal that body is light, the isolated carbonic oxide that contains, hydrogen, oxygen, combustible mixtures such as tar are biological fuel gas, contain the biological fuel gas of tar, after tar filtration unit purifying treatment, through pipeline circulating system, biological fuel gas is directly sent in the drying oven, as the drying machine thermal source; Another part biological fuel gas is delivered in the storage tank by pipeline circulating system.Main points of the present invention are its manufacture craft and comprehensive utilization.Its technological principle is, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process is with preparation back powdery biomass material, or bar-shaped biomass material, the charing in the biomass carbonated gasification combustion furnace of packing into, charring furnace utilizes the destructive distillation principle, makes the spontaneous combustion under anoxic condition of stove endogenous substance raw material, begins reduction when furnace temperature reaches preset temperature, cracking, generate energy conversion, isolates charcoal and inflammable gas, inflammable gas is handled through the tar purifying device, reclaims the back and uses.The biological fuel gas that preparation technology's method produces is to contain carbon monoxide (CO), the combustible mixture of hydrogen (H), oxygen (O), tar, the biological fuel gas that contains tar, after tar filtration unit purifying treatment, through pipeline circulating system, part biological fuel gas is directly sent in the drying oven, as the drying machine thermal source, produces used for our unit's drying machine; Another part biological fuel gas is transported in the gas-holder by pipeline circulating system, offers user's production or lives used; Because the operation 24 hours every days of biomass carbonated gasification combustion furnace, gas production rate is bigger, both can directly supply with the user and use, and can deposit in the gas-holder as used with gas peak peak regulation the corresponding capacity that reduces gas-holder again on a small quantity in.A kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process compared with prior art, have and be skillfully constructed, versatility, scientific and reasonable, creativity consciousness is arranged, easy to use, reduce expenses, cheap, improved the comprehensive utilization ratio of biomass renewable energy sources, changed and processed the necessary discharging waste gas of charcoal, contaminate environment, processing biological combustion gas in the past, the phenomenon that waste residue discharges nowhere, have and both saved biomass energy, improved advantages such as the social benefit and the performance of enterprises again, will be widely used in the renewable energy source domain.
Embodiment:
Embodiment one, its preparation technology is: at first the collection of biological raw material is a sawdust, wood shavings, branch, the wooden class raw material of trunk forestry waste, be processed into the 0.5-15mm powder through pulverizer, deposit in the feed bin standby, drying machine material loading winch is sent in the drying machine raw material dry, it is thermal source that drying oven adopts biological fuel gas, the byproduct that produces during the used comprehensive biomass solidifying, carbonizing and gasifying utilization process processing of its drying oven charcoal, it is biological fuel gas, raw material in the drying machine is behind drying and dewatering under 60 ℃ of-100 ℃ of temperature, under the induced draft fan effect, separate through separator, separator upper end vapour discharge and moisture, the lower end spills dried raw material, and the preparation method of charing is with the wooden class raw material of sawdust after its first moulding, after biomass forming machine squeezes out bar-like raw material, pack in the biomass carbonated gasification combustion furnace, under the temperature control effect, process high temperature high-quality machine-made charcoal and biological fuel gas; The preparation method of its first charing aftershaping packs wooden material powder in the biomass carbonated gasification combustion furnace into, generates black solid powdered carbon and biological fuel gas under the temperature control effect, and it is machine-made charcoal that powdered carbon is squeezed into carbon rod through biomass forming machine; The raw material water content does not surpass 12% can be dry; Elder generation's charing aftershaping is the tackiness agent that the powdered carbon after the charing processing is inserted 0.5%-5%, stir evenly, be squeezed into Φ 30 * 150mm through spiral biomass charcoal powder shaper, the hollow carbon rod of Φ 50 * 450mm specification, it is the common machine-made charcoal of low temperature, the rated pressure of carbon rod extrusion molding is 15mpa, and density is at 0.7-0.9g/mc 3Between, calorific value reaches that 6500-7000 kilocalorie/kilogram, carbon content reach 70%-75%, ash content reaches 6%-8%, is packaged into product; Charing is with the wooden class raw material of dried sawdust after elder generation's moulding, be squeezed into Φ 30 * 150mm through hydraulic biomass fuel forming machine or spiral biological substance fuel forming machine, the hollow bar-shaped raw material for standby of Φ 50 * 450mm specification, the rated pressure of bar extrusion molding is 15-31mpa, and density is at 0.8-1.2g/mc 3Between; Machine-shaping is biomass molding fuel without the bar of charing; Elder generation's charing aftershaping is that the raw material powder after the preparation is quantitative by 300-1000kg, the igniting back banking in the biomass carbonated gasification combustion furnace of packing into, the material powder is under anoxic condition spontaneous combustion 48-50 hour in the stove, produces water vapour and non-combustible gas when temperature in the stove reaches 150 ℃-300 ℃, in time discharges by discharge outlet, when temperature in the stove reaches 300 ℃-700 ℃, biomass are through reduction, cracking and polyreaction, and inflammable gas is isolated in the generate energy conversion, be biological fuel gas, recyclable; It is quantitative that the bar-like raw material of extrusion molding is pressed 500-2000kg, the igniting banking in back in the biomass carbonated gasification combustion furnace of packing into, produce water vapour and non-combustible gas when temperature reaches 150 ℃-430 ℃ in the bar under anoxic condition spontaneous combustion 48-50 hour, stove, in time discharge by discharge outlet; When temperature reached 430 ℃-900 ℃ in the stove, biomass were through reduction, cracking and polyreaction, and inflammable gas is isolated in the generate energy conversion, is biological fuel gas, and is recyclable; Bar through high-temperature calcination is the stronger high temperature high-quality machine-made charcoal of rigidity; Its calorific value reaches that 7500-8500 kilocalorie/kilogram, carbon content reach 80%-85%, ash content reaches 5-6%, is packaged into product; Biomass carbonated gasification combustion furnace endogenous substance is in the anoxycausis process, when reaching 150 ℃-430 ℃, temperature produces water vapour and non-combustible gas, in time discharge by discharge outlet, when temperature reaches 430 ℃-900 ℃, biomass begin reduction, cracking and polyreaction, the generate energy conversion, progressively separate, formation matter is hard, the black solid charcoal that body is light, the isolated carbonic oxide that contains, hydrogen, oxygen, combustible mixtures such as tar are biological fuel gas, contain the biological fuel gas of tar, after tar filtration unit purifying treatment, through pipeline circulating system, biological fuel gas is directly sent in the drying oven, as the drying machine thermal source; Another part biological fuel gas is delivered in the storage tank by pipeline circulating system.
Embodiment two, its preparation technology is: at first the collection of biological raw material is a sawdust, wood shavings, branch, the wooden material powder 50% of trunk forestry waste, maize straw, rice husk, faggot, corn cob, oil crops cot agricultural crop straw 50%, be processed into the 0.5-15mm powder through pulverizer, deposit in the feed bin standby, drying machine material loading winch is sent in the drying machine raw material dry, it is thermal source that drying oven adopts biological fuel gas, the byproduct that produces during the used comprehensive biomass solidifying, carbonizing and gasifying utilization process processing of its drying oven charcoal, it is biological fuel gas, raw material in the drying machine is behind drying and dewatering under 60 ℃ of-100 ℃ of temperature, under the induced draft fan effect, separate through separator, separator upper end vapour discharge and moisture, the lower end spills dried raw material, the preparation method of charing is with the raw material powder after the preparation after its first moulding, after biomass forming machine squeezes out bar-like raw material, pack in the biomass carbonated gasification combustion furnace, under the temperature control effect, process high temperature high-quality machine-made charcoal and biological fuel gas; The preparation method of its first charing aftershaping packs the raw material powder after the preparation in the biomass carbonated gasification combustion furnace into, generates black solid powdered carbon and biological fuel gas under the temperature control effect, and it is machine-made charcoal that powdered carbon is squeezed into carbon rod through biomass forming machine; The raw material water content does not surpass 12% can be dry; Elder generation's charing aftershaping is the tackiness agent that the powdered carbon after the charing processing is inserted 0.5%-5%, stir evenly, be squeezed into Φ 30 * 150mm through spiral biomass charcoal powder shaper, the hollow carbon rod of Φ 50 * 450mm specification, it is the common machine-made charcoal of low temperature, the rated pressure of carbon rod extrusion molding is 15mpa, and density is at 0.7-0.9g/mc 3Between, calorific value reaches that 6500-7000 kilocalorie/kilogram, carbon content reach 70%-75%, ash content reaches 6%-8%, is packaged into product; Charing is with the raw material powder after the preparation after elder generation's moulding, be squeezed into Φ 30 * 150mm through hydraulic biomass fuel forming machine or spiral biological substance fuel forming machine, the hollow bar-shaped raw material for standby of Φ 50 * 450mm specification, the rated pressure of bar extrusion molding is 15-31mpa, and density is at 0.8-1.2g/mc 3Between; Machine-shaping is biomass molding fuel without the bar of charing; Elder generation's charing aftershaping is that the raw material powder after the preparation is quantitative by 300-1000kg, the igniting back banking in the biomass carbonated gasification combustion furnace of packing into, the material powder is under anoxic condition spontaneous combustion 48-50 hour in the stove, produces water vapour and non-combustible gas when temperature in the stove reaches 150 ℃-300 ℃, in time discharges by discharge outlet, when temperature in the stove reaches 300 ℃-700 ℃, biomass are through reduction, cracking and polyreaction, and inflammable gas is isolated in the generate energy conversion, be biological fuel gas, recyclable; The biological fuel gas that contains tar, after tar filtration unit purifying treatment, through pipeline circulating system, biological fuel gas is directly sent in the drying oven, as the drying machine thermal source; Another part biological fuel gas is delivered in the storage tank by pipeline circulating system.

Claims (9)

1, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process, it is characterized in that: its preparation technology is, at first the collection of biological raw material is a sawdust, wood shavings, branch, the wooden class raw material of trunk forestry waste, be processed into the 0.5-15mm powder through pulverizer, deposit in the feed bin standby, drying machine material loading winch is sent in the drying machine raw material dry, it is thermal source that drying oven adopts biological fuel gas, the byproduct that produces during the used comprehensive biomass solidifying, carbonizing and gasifying utilization process processing of its drying oven charcoal, it is biological fuel gas, raw material in the drying machine is behind drying and dewatering under 60 ℃ of-100 ℃ of temperature, under the induced draft fan effect, separate separator upper end vapour discharge and moisture through separator, the lower end spills dried raw material, the preparation method of charing is with the wooden class raw material of sawdust after its first moulding, after biomass forming machine squeezes out bar-like raw material, in the biomass carbonated gasification combustion furnace of packing into, under the temperature control effect, process high temperature high-quality machine-made charcoal and biological fuel gas; The preparation method of its first charing aftershaping packs wooden material powder in the biomass carbonated gasification combustion furnace into, generates black solid powdered carbon and biological fuel gas under the temperature control effect, and it is machine-made charcoal that powdered carbon is squeezed into carbon rod through biomass forming machine.
2, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1 is characterized in that: said biomass material can be maize straw, rice husk, faggot, corn cob, oil crops cot agricultural crop straw.
3, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1 is characterized in that: said raw material water content does not surpass 12% can be dry.
4, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1 is characterized in that: said material powder can be wooden material powder 50%, straw material powder 50%.
5, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1, it is characterized in that: said first charing aftershaping is the tackiness agent that the powdered carbon after the charing processing is inserted 0.5%-5%, stir evenly, be squeezed into Ф 30 * 150mm through spiral biomass charcoal powder shaper, the hollow carbon rod of Ф 50 * 450mm specification, be the common machine-made charcoal of low temperature, the rated pressure of carbon rod extrusion molding is 15mpa, and density is at 0.7-0.9g/mc 3Between, calorific value reaches that 6500-7000 kilocalorie/kilogram, carbon content reach 70%-75%, ash content reaches 6%-8%, is packaged into product.
6, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1, it is characterized in that: charing is with the wooden class raw material of dried sawdust after the said first moulding, be squeezed into Ф 30 * 150mm through hydraulic biomass fuel forming machine or spiral biological substance fuel forming machine, the hollow bar-shaped raw material for standby of Ф 50 * 450mm specification, the rated pressure of bar extrusion molding is 15-31mpa, and density is at 0.8-1.2g/mc 3Between; Machine-shaping is biomass molding fuel without the bar of charing.
7, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1, it is characterized in that: said first charing aftershaping is that the raw material powder after the preparation is quantitative by 300-1000kg, the igniting back banking in the biomass carbonated gasification combustion furnace of packing into, the material powder is under anoxic condition spontaneous combustion 48-50 hour in the stove, when reaching 150 ℃-300 ℃, temperature in the stove produces water vapour and non-combustible gas, in time discharge by discharge outlet, when temperature in the stove reaches 300 ℃-700 ℃, biomass are through reduction, cracking and polyreaction, the generate energy conversion, isolating inflammable gas, is biological fuel gas, recyclable.
8, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1, it is characterized in that: it is quantitative that the bar-like raw material of said extrusion molding is pressed 500-2000kg, the igniting banking in back in the biomass carbonated gasification combustion furnace of packing into, bar under anoxic condition spontaneous combustion 48-50 hour, produce water vapour and non-combustible gas when temperature reaches 150 ℃-430 ℃ in the stove, in time discharge by discharge outlet; When temperature reached 430 ℃-900 ℃ in the stove, biomass were through reduction, cracking and polyreaction, and inflammable gas is isolated in the generate energy conversion, is biological fuel gas, and is recyclable; Bar through high-temperature calcination is the stronger high temperature high-quality machine-made charcoal of rigidity; Its calorific value reaches that 7500-8500 kilocalorie/kilogram, carbon content reach 80%-85%, ash content reaches 5-6%, is packaged into product.
9, a kind of comprehensive biomass solidifying, carbonizing and gasifying utilization process according to claim 1, it is characterized in that: biomass carbonated gasification combustion furnace endogenous substance is in the anoxycausis process, when reaching 150 ℃-430 ℃, temperature produces water vapour and non-combustible gas, in time discharge by discharge outlet, when temperature reaches 430 ℃-900 ℃, biomass begin reduction, cracking and polyreaction, the generate energy conversion, progressively separate, formation matter is hard, the black solid charcoal that body is light, the isolated carbonic oxide that contains, hydrogen, oxygen, combustible mixtures such as tar are biological fuel gas, the biological fuel gas that contains tar is after tar filtration unit purifying treatment, through pipeline circulating system, biological fuel gas is directly sent in the drying oven, as the drying machine thermal source; Another part biological fuel gas is delivered in the storage tank by pipeline circulating system.
CNA2006100459785A 2006-03-07 2006-03-07 Comprehensive biomass solidifying, carbonizing and gasifying utilization process Pending CN1810928A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2006100459785A CN1810928A (en) 2006-03-07 2006-03-07 Comprehensive biomass solidifying, carbonizing and gasifying utilization process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2006100459785A CN1810928A (en) 2006-03-07 2006-03-07 Comprehensive biomass solidifying, carbonizing and gasifying utilization process

Publications (1)

Publication Number Publication Date
CN1810928A true CN1810928A (en) 2006-08-02

Family

ID=36844049

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2006100459785A Pending CN1810928A (en) 2006-03-07 2006-03-07 Comprehensive biomass solidifying, carbonizing and gasifying utilization process

Country Status (1)

Country Link
CN (1) CN1810928A (en)

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101824347A (en) * 2009-03-06 2010-09-08 北京泛欧瑞德科技有限公司 Biomass composite granular fuel, and manufacturing method and device thereof
CN101050137B (en) * 2007-05-18 2010-12-22 中国林业科学研究院林业研究所 Synthesizing method and equipment for fabricating light ground substance by using farming and forestry biomass
CN102020999A (en) * 2010-12-30 2011-04-20 天津市树荣生物碳宝科技有限公司 Co-production equipment for preparing charcoal, gas and oil by utilizing various biomass materials and preparation method of charcoal, gas and oil
CN102240665A (en) * 2011-05-16 2011-11-16 杭州大清智能技术开发有限公司 Method for ecologically managing super-standard lead of tea garden soil
CN102358852A (en) * 2011-09-16 2012-02-22 天津德为环保工程设备有限公司 Production method for preparing agriculture and forestry plant wastes into biomass fuel lumps used for gas supply system through gasification
CN101629083B (en) * 2009-08-19 2013-01-23 北京林业大学 Treatment method of wood processing residues and charcoal prepared thereby
CN103173232A (en) * 2012-11-30 2013-06-26 徐学冬 Method for realizing intensive production and comprehensive utilization of forestry residues
CN103497774A (en) * 2013-09-30 2014-01-08 贵州省黎平县侗乡米业有限公司 Method for producing environment-friendly mechanism charcoal and coproducing wood tar oil and biogas by using anredera cordifolia
CN103614179A (en) * 2013-11-19 2014-03-05 梁万泉 Production process of high-effect transferred biomass particles
CN104087322A (en) * 2014-07-03 2014-10-08 黔西南州宏森木业有限公司 Method for preparing wood tar by using waste wood and saw dust
CN104629781A (en) * 2013-11-07 2015-05-20 永胜县益农新能源开发有限公司 Machine-made charcoal rod-making production system
CN104726158A (en) * 2013-12-25 2015-06-24 深圳德瑞新能科技有限公司 Method for producing compact biomass fuel at low energy consumption and high-quality compact biomass fuel
CN105199783A (en) * 2015-10-27 2015-12-30 北京神雾环境能源科技集团股份有限公司 Stock bin assembly and biomass gasification system
CN105459714A (en) * 2015-04-16 2016-04-06 郑启彬 Manufacturing method for charcoal artware
CN105665422A (en) * 2016-03-03 2016-06-15 何国华 Method for recycling stevioside waste residues or filter mud
CN107304365A (en) * 2016-04-21 2017-10-31 上海莱乾新能源有限公司 A kind of biomass intelligent ecological island
CN107828456A (en) * 2017-12-07 2018-03-23 福建山脉竹循环科技有限公司 A kind of Bamboo leftover multiplexer and method
CN109097078A (en) * 2018-09-21 2018-12-28 河南博顿生物科技有限公司 A kind of method that agricultural crop straw charing prepares biomass fuel
CN109836226A (en) * 2017-11-24 2019-06-04 陈燕蓉 A kind of charcoal base potato Slow release special fertilizer and preparation method thereof
CN111036173A (en) * 2019-11-26 2020-04-21 安吉竹墨新材料科技有限公司 Biomass charcoal-based activated coke and preparation method thereof
WO2023135445A1 (en) * 2022-01-13 2023-07-20 钟永康 Method for producing bio-coal

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101050137B (en) * 2007-05-18 2010-12-22 中国林业科学研究院林业研究所 Synthesizing method and equipment for fabricating light ground substance by using farming and forestry biomass
CN101824347A (en) * 2009-03-06 2010-09-08 北京泛欧瑞德科技有限公司 Biomass composite granular fuel, and manufacturing method and device thereof
CN101629083B (en) * 2009-08-19 2013-01-23 北京林业大学 Treatment method of wood processing residues and charcoal prepared thereby
CN102020999A (en) * 2010-12-30 2011-04-20 天津市树荣生物碳宝科技有限公司 Co-production equipment for preparing charcoal, gas and oil by utilizing various biomass materials and preparation method of charcoal, gas and oil
CN102020999B (en) * 2010-12-30 2013-08-07 天津市树荣生物碳宝科技有限公司 Co-production equipment for preparing charcoal, gas and oil by utilizing various biomass materials and preparation method of charcoal, gas and oil
CN102240665A (en) * 2011-05-16 2011-11-16 杭州大清智能技术开发有限公司 Method for ecologically managing super-standard lead of tea garden soil
CN102358852A (en) * 2011-09-16 2012-02-22 天津德为环保工程设备有限公司 Production method for preparing agriculture and forestry plant wastes into biomass fuel lumps used for gas supply system through gasification
CN103173232A (en) * 2012-11-30 2013-06-26 徐学冬 Method for realizing intensive production and comprehensive utilization of forestry residues
CN103497774A (en) * 2013-09-30 2014-01-08 贵州省黎平县侗乡米业有限公司 Method for producing environment-friendly mechanism charcoal and coproducing wood tar oil and biogas by using anredera cordifolia
CN104629781A (en) * 2013-11-07 2015-05-20 永胜县益农新能源开发有限公司 Machine-made charcoal rod-making production system
CN103614179A (en) * 2013-11-19 2014-03-05 梁万泉 Production process of high-effect transferred biomass particles
CN103614179B (en) * 2013-11-19 2015-07-15 深圳市草木新能源有限公司 Production process of high-effect transferred biomass particles
CN104726158A (en) * 2013-12-25 2015-06-24 深圳德瑞新能科技有限公司 Method for producing compact biomass fuel at low energy consumption and high-quality compact biomass fuel
CN104726158B (en) * 2013-12-25 2017-02-15 深圳德瑞新能科技有限公司 Method for producing compact biomass fuel at low energy consumption and high-quality compact biomass fuel
CN104087322A (en) * 2014-07-03 2014-10-08 黔西南州宏森木业有限公司 Method for preparing wood tar by using waste wood and saw dust
CN104087322B (en) * 2014-07-03 2016-05-11 黔西南州宏森木业有限公司 A kind of method of producing wood tar with waste wood and sawdust
CN105459714A (en) * 2015-04-16 2016-04-06 郑启彬 Manufacturing method for charcoal artware
CN105199783A (en) * 2015-10-27 2015-12-30 北京神雾环境能源科技集团股份有限公司 Stock bin assembly and biomass gasification system
CN105665422A (en) * 2016-03-03 2016-06-15 何国华 Method for recycling stevioside waste residues or filter mud
CN107304365A (en) * 2016-04-21 2017-10-31 上海莱乾新能源有限公司 A kind of biomass intelligent ecological island
CN109836226A (en) * 2017-11-24 2019-06-04 陈燕蓉 A kind of charcoal base potato Slow release special fertilizer and preparation method thereof
CN107828456A (en) * 2017-12-07 2018-03-23 福建山脉竹循环科技有限公司 A kind of Bamboo leftover multiplexer and method
CN109097078A (en) * 2018-09-21 2018-12-28 河南博顿生物科技有限公司 A kind of method that agricultural crop straw charing prepares biomass fuel
CN111036173A (en) * 2019-11-26 2020-04-21 安吉竹墨新材料科技有限公司 Biomass charcoal-based activated coke and preparation method thereof
WO2023135445A1 (en) * 2022-01-13 2023-07-20 钟永康 Method for producing bio-coal

Similar Documents

Publication Publication Date Title
CN1810928A (en) Comprehensive biomass solidifying, carbonizing and gasifying utilization process
CN101302430B (en) Method for preparing gas with crop wastes and organic refuses
CN105969467A (en) Biomass briquette fuel produced by performing anaerobic fermentation and modification on corn straws and production method thereof
CN105969453A (en) Low-chlorine value biomass briquette fuel and production method thereof
WO2008111766A1 (en) Apparatus and method for making fuel using forest residue
CN110591743A (en) Device and method for producing carbon by pyrolysis of rural biomass and integrating heat
CN105969454A (en) Anti-slagging biomass briquette fuel and production method thereof
CN101020344B (en) Process and apparatus for producing stalk honeycomb briquet
CN105969465A (en) Biomass briquette fuel with good bonding ability and fast moulding and production method thereof
CN106244282A (en) A kind of high fuel value sawdust based biomass granule and preparation method thereof
CN105969460A (en) Environmental protection-type high-calorific value biomass briquette fuel and production method thereof
CN105969470A (en) Lightweight carbon fiber biomass briquette fuel and production method thereof
CN109161424A (en) A kind of biomass synthetic fuel and preparation method thereof
CN101787377A (en) Method for preparing biomass straw biogas and adopted devices thereof
CN101775298A (en) Method for improving intensity and density of ecological carbon
CN103074113B (en) Method for preparing gas by using biomass and coal
Liu et al. Research progress of biomass fuel upgrading and distributed utilization technology
CN105969462A (en) High-combustion efficiency aerated biomass briquette fuel and production method thereof
CN111876177A (en) Method for preparing biofuel by co-pyrolysis of biomass and waste plastics
CN105861092A (en) Environment-friendly biomass pellet fuel
CN105670662A (en) Environment-friendly charcoal and preparing method thereof
CN106833795A (en) A kind of biomass composite fuel of utilization wild rice stem shell and preparation method thereof
CN105861567A (en) Method for producing high-heating-value biomass fuel from agricultural and forestry wastes
CN106244284A (en) A kind of sawdust based biomass granule of volume length little burning time and preparation method thereof
CN111303956A (en) Clean and efficient biomass fuel and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication