CN1710022A - Method for producing biomass carbonized gas and back fire-biomass carbonated gas generating stove - Google Patents
Method for producing biomass carbonized gas and back fire-biomass carbonated gas generating stove Download PDFInfo
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- CN1710022A CN1710022A CNA2005100408401A CN200510040840A CN1710022A CN 1710022 A CN1710022 A CN 1710022A CN A2005100408401 A CNA2005100408401 A CN A2005100408401A CN 200510040840 A CN200510040840 A CN 200510040840A CN 1710022 A CN1710022 A CN 1710022A
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Abstract
Its craft steps are: respectively cut material into pieces, comminute, and filtrate, add material unsuitable to produce carbonization into the upper layer converse fire gasifying stove cavity as its gasifying fuel; add gasifying material suitable for producing biomass charcoal into the carbonizing stove cavity equipped on the nether layer; produce biomass fuel gas and get biomass carbonized products. Its main structure is: there equips upper layer converse fire gasifying stove cavity and nether layer carbonizing stove cavity in the stove body. Its advantages are: its biomass carbonized fuel gas value can get to 5000 - 6000 KJ/h, add the produced biomass charcoal into water-soluble macromolecule cementing agent after comminuted to process into machine-made charcoal by mechanism extrusion; it can replace the carbonized produces of previous wood charcoal; its structure is simple and reasonable, and is convenient to operate; besides its processing material quantity is large, carbonization speed in stove is high and its efficiency is high.
Description
Technical field
What the present invention relates to is a kind of method and back fire-biomass carbonated gas generating stove of producing biological fuel gas and biomass charcoal in the anti-internal heat furnace chamber in the upper strata that is arranged and the lower floor's charing furnace chamber that agriculture and forestry organic waste materials such as biomass straw, branch, rice husk, shell are divided in same stove.Belong to the back fire-biomass carbonated gas generating stove technical field.
Background technology
Also do not find as yet in the prior art in same stove, to divide method and the back fire-biomass carbonated gas generating stove of producing biological fuel gas and biomass charcoal in the anti-internal heat furnace chamber in the upper strata that is arranged and the lower floor's charing furnace chamber with agriculture and forestry organic waste materials such as biomass straw, branch, rice husk, shells.
Summary of the invention
Purpose of the present invention is proposing a kind of method and back fire-biomass carbonated gas generating stove that adopts back fire-biomass carbonated gas generating stove to produce biomass charcoal again in the production biological fuel gas.Specifically, be a kind of with above-mentioned material through chopping or pulverize, after oven dry is handled, add and divide the anti-internal heat furnace chamber in upper strata and the lower floor's charing furnace chamber that is arranged in the stove, make earlier and add the reaction of the material generating gasification in the anti-internal heat furnace chamber in upper strata in the stove, produce 300～500 ℃ biomass combustible gas, and simultaneously inflammable gas is sucked lower floor's charing furnace chamber in the stove and come the material production biological fuel gas in the destructive distillation lower floor charing furnace chamber and the method for biomass charcoal.The biomass charcoal of Sheng Chaning in this way, carbon content height, ash are few, and be mutually basic with the composition of conventional wooden charcoal, is both a kind of ideal carbo lignius substitute products.Technical solution of the present invention: the method for producing biomass carbonated gas, its processing step is divided into: one, with agriculture and forestry organic waste materials such as biomass straw, branch, rice husk, shells through chipping or pulverizing, material after the chopping is removed dirt wherein and is not met the waste material that is used to produce biomass charcoal again through Screening Treatment;
Two, will after screening, not meet to add after the waste material of producing biomass charcoal carries out processing treatment and be arranged in the stove in the anti-internal heat furnace chamber in upper strata, be used as the vaporising fuel in the anti-internal heat furnace chamber in upper strata in the stove;
Three, will meet the material adding of producing the biomass charcoal requirement is arranged in the interior lower floor of the stove charing furnace chamber;
Four, when operation the gasification materiel in the upper strata gasification furnace chamber in the ignition furnace at first, and start sucktion fan, make air (vaporized chemical) from last fire door enter in the stove the upper strata gasification furnace chamber with the gasification furnace chamber in gasification materiel carry out gasification reaction and generate CO, H
2, CH
4, 300～500 ℃ of CmHmm etc. inflammable gas enter the material that comes in the charing furnace chamber that is arranged on lower floor in the stove in the dry distillation charring furnace chamber simultaneously, in lower floor's charing furnace chamber in the dry distillation charring material, make the charing material discharge wherein fugitive constituent hydro carbons golf calorific value material from the anti-internal heat furnace chamber in upper strata with after the inflammable gas that enters mixes, in the calorific value inflammable gas be sucked come out of the stove outside;
Five, 300～500 ℃ of inflammable gass that produce in the anti-internal heat furnace chamber in upper strata in stove enter in the stove behind lower floor's charing furnace chamber, make the material in the charing furnace chamber be become biomass charcoal by dry distillation charring, discharge out of the furnace by the discharge port that is arranged on the bottom of lower floor's charing furnace chamber in the stove again, biomass carbonated product;
Back fire-biomass carbonated gas generating stove, its structure is to be provided with the anti-internal heat furnace chamber in upper strata and lower floor's charing furnace chamber in the body of heater, the anti-internal heat furnace chamber in upper strata and lower floor's charing furnace chamber intermediate section are not provided with explosion-proof mouth of pipe joint and charing furnace chamber charging opening in the stove, and the body of heater bottom is provided with the body of heater pillar stiffener.
Advantage of the present invention:, can make the biological fuel gas calorific value up to 5000～6000kj/m 1, through using back fire-biomass carbonated gas generating stove
3, produce biological fuel gas calorific value (4000～5000kj/m than existing various stalk pyrolytic gasification stoves
3) improve about 30%, will use biological flue gas for the town dweller burns, and can dwindle the combustion gas caliber, thereby reduce the pipe-networks engineering investment and save engineering materials.2, can be used for producing the carbonated material of gac through biomass charcoal, can be widely used in the municipal sewage treatment recycling, alleviate the contradiction of present numerous city water resource shortage with this explained hereafter.3, add the water-soluble polymer binding agent after crushed through biomass charcoal and be processed into machine-made carbon, substitute former carbonization product, can be widely used in fields such as industry, chemical industry, metallurgy and environment protection with carbo lignius with mechanical presses with this explained hereafter.4, the abundant agricultural waste resource in the vast rural area of regeneration China, the management that not only helps country to strengthen closing hillsides to facilitate afforestation for preventing erosion, and can make human the minimizing to using the dependence of fossil fuel (coal, oil, Sweet natural gas), the exhausted time that can favourablely delay the fossil fuel resource is very important.5, make full use of the annual agriculture and forestry organic waste material that produces several hundred million tons in rural area; not only can strengthen the rural ecological environment protection but also to save energy; increase farmers' income, development rural area recycling economy, to improve social synthesis's benefit such as town dweller's quality of life also very remarkable.6, back fire-biomass carbonated gas generating stove of the present invention is simple and reasonable, and operation is convenient, and the material handling amount is big, the interior charing rate of stove is fast, efficient is high, is convenient to large-scale industrial production.
Description of drawings
Accompanying drawing is the structural representation of back fire-biomass carbonated gas generating stove.
Among the figure 1 is upper strata anti-internal heat furnace chamber charging opening, the 2nd, the upper strata furnace roof, the 3rd, rotation axis in the anti-internal heat furnace chamber in upper strata, the 4th, weed the material bar in the anti-internal heat furnace chamber in upper strata, the 5th, the anti-internal heat furnace chamber in upper strata, the 6th, anti-internal heat furnace chamber bottom, upper strata ash exhauster, the 7th, upper strata anti-internal heat furnace chamber ash discharge auger sleeve pipe, the 8th, lower floor's charing furnace chamber weeds the material bar in the stove, the 9th, the explosion-proof mouth of pipe joint of body of heater, the 10th, lower floor's charing furnace chamber in the stove, the 11st, the body of heater refractory lining, the 12nd, water jacket of the furnace body, the 13rd, lower floor's charing furnace chamber biological fuel gas outlet pipe connection, the 14th, rotation axis in lower floor's charing furnace chamber, the 15th, the body of heater pillar stiffener, the 16th, lower floor charing furnace chamber bottom goes out charcoal mouth of pipe joint, the 17th, lower floor's tapered water jacket collection charcoal case in charing furnace chamber bottom, the 18th, lower floor charing furnace chamber bottom goes out the charcoal device, the 19th, the charing furnace chamber row of lower floor charcoal device, the 20th, lower floor's charing furnace chamber manhole, the 21st, lower floor's charing furnace chamber filling tube mouth, the 22nd, the tapered dust collecting box of upper strata gasification furnace chamber, the 23rd, anti-internal heat furnace chamber bottom, upper strata ash discharging gear, the 24th, the anti-internal heat furnace chamber in the upper strata circle of bleeding.
Embodiment
The contrast accompanying drawing, its structure is to be provided with the anti-internal heat furnace chamber 5 in upper strata and lower floor's charing furnace chamber 10 in the body of heater, the centre of the anti-internal heat furnace chamber 5 in upper strata and lower floor's charing furnace chamber 10 is respectively equipped with explosion-proof mouth of pipe joint 9 and charing furnace chamber filling tube mouth 21 in the stove, and the body of heater bottom is provided with body of heater pillar stiffener 15.
The top of the upper strata furnace roof 2 in the anti-internal heat furnace chamber 5 in upper strata is provided with upper strata anti-internal heat furnace chamber charging opening 1 in the stove, the central authorities of anti-internal heat furnace chamber 5 are provided with upper strata anti-internal heat furnace chamber rotation axis 3 on the upper strata, the bottom of the anti-internal heat furnace chamber 5 in upper strata is provided with anti-internal heat furnace chamber bottom, upper strata ash discharging gear 23, anti-internal heat furnace chamber bottom, upper strata ash exhauster 6 is located on the ash discharging gear 23 of anti-internal heat furnace chamber bottom, upper strata, be provided with body of heater refractory lining 11 in the stove in the anti-internal heat furnace chamber 5 in upper strata or build by laying bricks or stones with lower floor charing furnace chamber 10 and be connected with refractory brick, be provided with in the anti-internal heat furnace chamber in upper strata rotation axis 3 in the anti-internal heat furnace chamber 5 in upper strata and weed material bar 4 and link with anti-internal heat furnace chamber bottom, upper strata ash exhauster 6, ash discharging gear 23 bottoms, anti-internal heat furnace chamber bottom, upper strata are established the upper strata gasification tapered dust collecting box 22 of furnace chamber and are provided with upper strata anti-internal heat furnace chamber ash discharge auger sleeve pipe 7 in the bottom of the tapered dust collecting box 22 of upper strata gasification furnace chamber.
Bottom at lower floor's charing furnace chamber 10 is provided with out charcoal device 18 successively, tapered water jacket collection charcoal case 17, the top that goes out charcoal device 18 connects the charing furnace chamber row of lower floor charcoal device 19, be provided with suction stove internal combustion gas tube orifice joint 13 in lower floor's tapered water jacket collection charcoal case 17 in charing furnace chamber bottom and go out charcoal mouth of pipe joint 16, be provided with body of heater refractory lining 11 in lower floor's charing furnace chamber 10 or build by laying bricks or stones with the anti-internal heat furnace chamber 5 in upper strata and be connected with refractory brick, in lower floor's charing furnace chamber that the central authorities of lower floor's charing furnace chamber 10 are provided with rotation axis 14 and lower floor charing furnace chamber 10 bottoms go out charcoal device 18 and the charing furnace chamber row of lower floor charcoal device 19 links.
Working process:
With maize straw, rice husk is a main raw material, by above-mentioned craft screening, remove dirt wherein and do not meet and be used as the waste material that the carbonization material requires, after the drying dehydration, moisture content is controlled at about 15%, add high 7.9 meters, in the interior lower floor of the above-mentioned stove that interior diameter the is 2 meters charing furnace chamber 10, the above screen underflow fines that is used as the charing material and other agriculture and forestry organic waste material etc. of not meeting are added in the stove after processing treatment and ignite in the anti-internal heat furnace chamber 5 in upper strata, start sucktion fan, air (vaporized chemical) charging opening 1 from stove is sucked in the stove the upper strata gasification furnace chamber 5 carry out gasification reaction and produce 300～500 ℃ inflammable gas and in stove, be pumped to outside the stove in lower floor's charing furnace chamber 10 again with gasification materiel, make in the stove material in lower floor's charing furnace chamber 10 because of being entered 300～500 ℃ of inflammable gas destructive distillation simultaneously, the fugitive constituent hydro carbons golf calorific value material that discharges wherein mixes with the inflammable gas that enters lower floor's charing furnace chamber 10 from the anti-internal heat furnace chamber 5 in upper strata, and its fuel gases calorific value can be up to 5000～6000kj/m
3Material in the stove in lower floor's charing furnace chamber 10 is behind 300～500 ℃ of inflammable gas dry distillation charrings, discharge the bottom carbon outleting port 16 of biomass charcoal lower floor's charing furnace chamber 10 in stove, add the water-soluble polymer binding agent after crushed, be processed into the machine-made carbon product with mechanical presses, its intensity and external form all are better than the conventional wooden charcoal, reach the standard of machine-processed forming charcoal.
This stove per hour consumes above-mentioned material 1350kg/h, wherein, is used for the gasification materiel 600kg/h of gasification furnace chamber in upper strata in the stove, produces 5000～6000kj/m
3Biomass combustible gas, be used for the charing material 750kg/h of lower floor's charing furnace chamber in the stove, can produce biomass charcoal 230～250kg/h, and can produce biological fuel gas 1000m simultaneously
3/ h, charcoal ash 90kkgh.
Adopt back fire-biomass carbonated gas generating stove to produce the method for biomass charcoal and biological fuel gas:
Embodiment 1
With corn stalk, the jowar straw is a main raw material, after above-mentioned technology chopping, screening is removed dirt wherein and is not met and is used as the waste material that the charing material requires, after the drying dehydration then, water ratio is controlled at 15%, add high 8.9 meters, in the interior lower floor of the above-mentioned stove that interior diameter the is 3 meters charing furnace chamber 10, after processing treatment, do not add in the stove and ignite in the upper strata gasification furnace chamber 5 meeting the screen underflow straw fines that is used as the charing material and other agriculture and forestry organic waste material etc., start sucktion fan with air (vaporized chemical), charging opening 1 is pumped into the inflammable gas that carries out 300-500 ℃ of gasification reaction generation the anti-internal heat furnace chamber 5 in stove upper strata with gasification materiel from stove, in stove, be pumped to outside the stove in lower floor's charing furnace chamber 10 again, the charing material that makes lower floor charing chamber 10 in the stove simultaneously is because of being entered 300-500 ℃ of inflammable gas destructive distillation, discharge wherein fugitive constituent hydro carbons golf calorific value material and in stove the anti-internal heat furnace chamber 5 in upper strata enter that the mixed fuel gases calorific value of inflammable gas can be up to 5000-6000kj/m lower floor's charing furnace chamber 10 in the stove
3Charing material in lower floor's charing furnace chamber 10 in the stove is promptly generated behind 300-500 ℃ of inflammable gas dry distillation charring the bottom carbon outleting port 16 of biomass charcoal lower floor's charing furnace chamber 10 in stove discharges, add the water-soluble polymer binding agent after crushed and be processed into the machine-made carbon product with mechanical presses, its intensity and external form all are better than the standard that the conventional wooden charcoal reaches machine-processed forming charcoal.
This stove per hour consumes above-mentioned material 3500kg/h, wherein, is used for the gasification materiel 1500kg/h of the anti-internal heat furnace chamber in upper strata in the stove, produces 5000-6000kj/m
3Biomass combustible gas, be used for the charing material 2000kg/h of lower floor's charing furnace chamber in the stove, can produce biomass charcoal 600kg/h, and can produce biological fuel gas 2500m simultaneously
3/ h, charcoal ash 225kg/h.
With branch, cotton stalk is a main raw material, after above-mentioned technology chopping, screening is removed wherein dirt and is not met the waste material that is used as the requirement of charing material, after the drying dehydration then, water ratio is controlled at 15%, add high 9.6 meters again, in the interior lower floor of the above-mentioned stove that interior diameter the is 3.6 meters charing furnace chamber 10, with the above-mentioned screen underflow that is used as the charing material that do not meet, branch, fines such as cotton stalk and other agriculture and forestry organic waste material add after processing treatment and ignite in the anti-internal heat furnace chamber 5 in upper strata in the stove, start sucktion fan with air (vaporized chemical), from stove charging opening 1 be pumped into the anti-internal heat furnace chamber 5 in stove upper strata with the gasification furnace chamber in gasification materiel carry out gasification reaction and produce 300-500 ℃ inflammable gas, in stove, be pumped to outside the stove in lower floor's charing furnace chamber 10 again, make the charing material in lower floor's charing furnace chamber 10 in the stove simultaneously because of being entered 300-500 ℃ of inflammable gas destructive distillation and discharge fugitive constituent hydro carbons golf calorific value material wherein and the anti-internal heat furnace chamber 5 in upper strata enters lower floor's charing furnace chamber 10 in stove the mixed fuel gases calorific value of inflammable gas can be up to 5000-6000kj/m
3Make simultaneously the material in the charing furnace chamber 10 in the stove after 300-500 ℃ inflammable gas dry distillation charing discharge the bottom carbon outleting port 16 of biomass charcoal lower floor's charing furnace chamber 10 in stove, add the water-soluble polymer binding agent after crushed and be processed into the machine-made carbon product with mechanical presses, its intensity and external form all are better than the standard that the conventional wooden charcoal reaches machine-made carbon.
This stove per hour consumes above-mentioned material 5000kg/h, wherein, is used for the gasification materiel 2000kg/h of gasification furnace chamber in upper strata in the stove, produces 5000-6000kj/m
3Biomass combustible gas is used for the charing material 3000kg/h of lower floor's charing furnace chamber in the stove, can produce biomass charcoal 900-1000kg/h, and can produce biological fuel gas 3500m simultaneously
3/ h, charcoal ash 300kg/h.
Claims (4)
1, produces the method for biomass carbonated gas, the processing step that it is characterized in that it is divided into: one, with agriculture and forestry organic waste materials such as biomass straw, branch, rice husk, shells through chipping or pulverizing, material after the chopping is removed dirt wherein and is not met the waste material that is used to produce biomass charcoal again through Screening Treatment; Two, will after screening, not meet to add after the material of producing biomass charcoal carries out processing treatment and be arranged in the stove in the anti-internal heat furnace chamber in upper strata, be used as the vaporising fuel in the anti-internal heat furnace chamber in upper strata in the stove; Three, will meet the material adding of producing the biomass charcoal requirement is arranged in the interior lower floor of the stove charing furnace chamber; Four, when operation the gasification materiel in the anti-internal heat furnace chamber in upper strata in the ignition furnace at first, and start sucktion fan, make air (vaporized chemical) from last fire door enter in the stove the anti-internal heat furnace chamber in upper strata with the gasification furnace chamber in gasification materiel carry out gasification reaction and generate CO, H
2, CH
4, 300～500 ℃ of CmHmm inflammable gas enter the material that comes in the charing furnace chamber that is arranged on lower floor in the stove in the dry distillation charring furnace chamber simultaneously, after the inflammable gas that enters fugitive constituent hydro carbons quantity of material occurred frequently that the charing material discharges it and the anti-internal heat furnace chamber from the upper strata is mixed, in the calorific value inflammable gas be sucked come out of the stove outside; Five, 300～500 ℃ of inflammable gass that produce in the anti-internal heat furnace chamber in upper strata in stove enter in the stove behind lower floor's charing furnace chamber, make the material in the charing furnace chamber be become biomass charcoal by dry distillation charring, discharge out of the furnace by the discharge port that is arranged on the bottom of lower floor's charing furnace chamber in the stove again, biomass carbonated product.
2, back fire-biomass carbonated gas generating stove, it is characterized in that being provided with in the body of heater the anti-internal heat furnace chamber in upper strata (5) and lower floor's charing furnace chamber (10), be respectively equipped with explosion-proof mouth of pipe joint (9) and charing furnace chamber charging opening (21) in the stove in the middle of the anti-internal heat furnace chamber in upper strata (5) and the lower floor's charing furnace chamber (10), the body of heater bottom is provided with body of heater pillar stiffener (15).
3, back fire-biomass carbonated gas generating stove according to claim 2, the top that it is characterized in that the upper strata furnace roof (2) in the anti-internal heat furnace chamber in upper strata (5) is provided with upper strata anti-internal heat furnace chamber charging opening (1) in the stove, the central authorities of anti-internal heat furnace chamber (5) are provided with upper strata anti-internal heat furnace chamber rotation axis (3) on the upper strata, the bottom of the anti-internal heat furnace chamber in upper strata (5) is provided with anti-internal heat furnace chamber bottom, upper strata ash discharging gear (23), the anti-internal heat furnace chamber bottom ash exhauster in upper strata (6) is located on the anti-internal heat furnace chamber bottom ash discharging gear in upper strata (23), be provided with body of heater refractory lining (11) in the anti-internal heat furnace chamber in upper strata (5) in the stove or build by laying bricks or stones with lower floor's charing furnace chamber (10) and be connected with refractory brick, weed material bar (4) in the anti-internal heat furnace chamber in the upper strata of establishing in the anti-internal heat furnace chamber in upper strata (5) and link with the anti-internal heat furnace chamber bottom ash exhauster in upper strata (6), the bottom that the bottom of the anti-internal heat furnace chamber bottom ash discharging gear in upper strata (23) is provided with upper strata gasification tapered dust collecting box of furnace chamber (22) and the upper strata gasification tapered dust collecting box of furnace chamber (22) is provided with upper strata anti-internal heat furnace chamber ash discharge auger sleeve pipe (7)
4, back fire-biomass carbonated gas generating stove according to claim 2, it is characterized in that being provided with out charcoal device (18) successively in the bottom of lower floor's charing furnace chamber (10), tapered water jacket collection charcoal case (17), the top that goes out charcoal device (18) connects the charing furnace chamber row of lower floor charcoal device (19), be provided with suction stove internal combustion gas tube orifice joint (13) in lower floor's charing furnace chamber tapered water jacket collection charcoal case in bottom (17) and go out charcoal mouth of pipe joint (16), be provided with body of heater refractory lining (11) in lower floor's charing furnace chamber (10) or build by laying bricks or stones with the anti-internal heat furnace chamber in upper strata (5) and be connected with refractory brick, be provided with in lower floor's charing furnace chamber in the central authorities of lower floor's charing furnace chamber (10) that the bottom of rotation axis (14) and lower floor's charing furnace chamber (10) goes out charcoal device (18) and lower floor's charing furnace chamber row's charcoal device (19) links.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100408401A CN100340634C (en) | 2005-07-01 | 2005-07-01 | Method for producing biomass carbonized gas and back fire-biomass carbonated gas generating stove |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100408401A CN100340634C (en) | 2005-07-01 | 2005-07-01 | Method for producing biomass carbonized gas and back fire-biomass carbonated gas generating stove |
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| Publication Number | Publication Date |
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| CN1710022A true CN1710022A (en) | 2005-12-21 |
| CN100340634C CN100340634C (en) | 2007-10-03 |
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| CNB2005100408401A Expired - Fee Related CN100340634C (en) | 2005-07-01 | 2005-07-01 | Method for producing biomass carbonized gas and back fire-biomass carbonated gas generating stove |
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| CN (1) | CN100340634C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101838555A (en) * | 2010-05-20 | 2010-09-22 | 赵学忠 | Producer for coproducing gas, carbon and liquid of biomass |
| CN102002399A (en) * | 2010-11-15 | 2011-04-06 | 国电长源电力股份有限公司 | Fluidized bed gasification reaction method and reactor employing packed fuel |
| CN103614179A (en) * | 2013-11-19 | 2014-03-05 | 梁万泉 | Production process of high-effect transferred biomass particles |
| CN107384485A (en) * | 2017-09-21 | 2017-11-24 | 南京林业大学 | The gas-carbon cogeneration device of ature of coal particle fixed bed gasification |
| CN113430012A (en) * | 2021-05-07 | 2021-09-24 | 章兴荣 | Organic solid waste recycling method |
| US11370982B2 (en) * | 2016-08-30 | 2022-06-28 | Thermochem Recovery International, Inc. | Method of producing liquid fuel from carbonaceous feedstock through gasification and recycling of downstream products |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4404673C2 (en) * | 1994-02-15 | 1995-11-23 | Entec Recycling Und Industriea | Process for the production of fuel gas |
| CN1116383C (en) * | 2000-11-22 | 2003-07-30 | 中国科学技术大学 | Composite biomass gasification furnace and its gas preparation method |
| CN1632060A (en) * | 2004-11-24 | 2005-06-29 | 韩璋鑫 | Method for producing biomass charcoal and charring furnace with double furnace chambers therefor |
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2005
- 2005-07-01 CN CNB2005100408401A patent/CN100340634C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101838555A (en) * | 2010-05-20 | 2010-09-22 | 赵学忠 | Producer for coproducing gas, carbon and liquid of biomass |
| CN101838555B (en) * | 2010-05-20 | 2012-10-17 | 赵学忠 | Producer for coproducing gas, carbon and liquid of biomass |
| CN102002399A (en) * | 2010-11-15 | 2011-04-06 | 国电长源电力股份有限公司 | Fluidized bed gasification reaction method and reactor employing packed fuel |
| 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 |
| US11370982B2 (en) * | 2016-08-30 | 2022-06-28 | Thermochem Recovery International, Inc. | Method of producing liquid fuel from carbonaceous feedstock through gasification and recycling of downstream products |
| US11634650B2 (en) | 2016-08-30 | 2023-04-25 | Thermochem Recovery International, Inc. | Method of producing liquid fuel from carbonaceous feedstock through gasification and recycling of downstream products |
| CN107384485A (en) * | 2017-09-21 | 2017-11-24 | 南京林业大学 | The gas-carbon cogeneration device of ature of coal particle fixed bed gasification |
| CN107384485B (en) * | 2017-09-21 | 2022-12-02 | 南京林业大学 | Gas-carbon co-production device for fixed bed gasification of coal particles |
| CN113430012A (en) * | 2021-05-07 | 2021-09-24 | 章兴荣 | Organic solid waste recycling method |
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| Publication number | Publication date |
|---|---|
| CN100340634C (en) | 2007-10-03 |
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