RU2012148762A - Способ торрефикации - Google Patents
Способ торрефикации Download PDFInfo
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- RU2012148762A RU2012148762A RU2012148762/04A RU2012148762A RU2012148762A RU 2012148762 A RU2012148762 A RU 2012148762A RU 2012148762/04 A RU2012148762/04 A RU 2012148762/04A RU 2012148762 A RU2012148762 A RU 2012148762A RU 2012148762 A RU2012148762 A RU 2012148762A
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- Prior art keywords
- biomass material
- chamber
- torrefaction
- stage
- fluid
- Prior art date
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- 238000000034 method Methods 0.000 title claims abstract 33
- 239000002028 Biomass Substances 0.000 claims abstract 25
- 239000000463 material Substances 0.000 claims abstract 22
- 239000012530 fluid Substances 0.000 claims abstract 12
- 239000007789 gas Substances 0.000 claims abstract 9
- 239000002551 biofuel Substances 0.000 claims abstract 6
- 239000002023 wood Substances 0.000 claims abstract 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract 2
- 238000010438 heat treatment Methods 0.000 claims abstract 2
- 239000011261 inert gas Substances 0.000 claims abstract 2
- 239000001301 oxygen Substances 0.000 claims abstract 2
- 229910052760 oxygen Inorganic materials 0.000 claims abstract 2
- 239000003245 coal Substances 0.000 claims 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- 238000005054 agglomeration Methods 0.000 claims 1
- 230000002776 aggregation Effects 0.000 claims 1
- 238000010924 continuous production Methods 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000002203 pretreatment Methods 0.000 claims 1
- 238000007873 sieving Methods 0.000 claims 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/447—Carbonized vegetable substances, e.g. charcoal, or produced by hydrothermal carbonization of biomass
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
- C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
- C10B49/08—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
- C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
- C10B49/08—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form
- C10B49/12—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form by mixing tangentially, e.g. in vortex chambers
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
- C10L5/08—Methods of shaping, e.g. pelletizing or briquetting without the aid of extraneous binders
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/363—Pellets or granulates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/366—Powders
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
- C10L9/083—Torrefaction
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/10—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers
- F26B17/107—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers pneumatically inducing within the drying enclosure a curved flow path, e.g. circular, spiral, helical; Cyclone or Vortex dryers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/02—Biomass, e.g. waste vegetative matter, straw
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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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Sustainable Development (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
1. Способ торрефикации биомассы для получения биотоплива, включающий:(i) торрефикацию материала биомассы в реакторе с тороидальным слоем, который имеет реакционную камеру с потоком текучей среды, направляемым в целом по окружности камеры для обеспечения быстрого вращения материала биомассы вокруг оси реакционной камеры в зоне, имеющей тороидальную форму, и для нагрева материала биомассы, причем текучая среда содержит газ или газы, вводимые в реакционную камеру, в которой поддерживается среда с низким содержанием кислорода.2. Способ по п.1, в котором газ или газы содержат перегретый пар и/или инертный газ.3. Способ по п.1 или 2, в котором материал биомассы содержит древесину или продукты переработки древесины.4. Способ по п.1 или 2, в котором на стадии (i) торрефикации материал биомассы нагревают до температуры от 280°С до 400°С.5. Способ по п.4, в котором на стадии (i) торрефикации материал биомассы нагревают до температуры от 320°С до 350°С.6. Способ по пп.1, 2 или 5, в котором время пребывания материала биомассы в реакторе с тороидальным слоем на стадии (i) не превышает 5 мин.7. Способ по п.6, в котором время пребывания материала биомассы в реакторе с тороидальным слоем на стадии (i) не превышает 60 с.8. Способ по пп.1, 2, 5 или 7, в котором поток текучей среды внутри реакционной камеры имеет горизонтальную и вертикальную составляющие скорости.9. Способ по пп.1, 2, 5 или 7, в котором камера имеет множество наклонных отходящих наружу впускных отверстий для текучей среды в основании камеры или возле него, причем текучая среда направляется через впускные отверстия в основании камеры для формирования внутри нее кругового потока текучей среды.10. Способ
Claims (21)
1. Способ торрефикации биомассы для получения биотоплива, включающий:
(i) торрефикацию материала биомассы в реакторе с тороидальным слоем, который имеет реакционную камеру с потоком текучей среды, направляемым в целом по окружности камеры для обеспечения быстрого вращения материала биомассы вокруг оси реакционной камеры в зоне, имеющей тороидальную форму, и для нагрева материала биомассы, причем текучая среда содержит газ или газы, вводимые в реакционную камеру, в которой поддерживается среда с низким содержанием кислорода.
2. Способ по п.1, в котором газ или газы содержат перегретый пар и/или инертный газ.
3. Способ по п.1 или 2, в котором материал биомассы содержит древесину или продукты переработки древесины.
4. Способ по п.1 или 2, в котором на стадии (i) торрефикации материал биомассы нагревают до температуры от 280°С до 400°С.
5. Способ по п.4, в котором на стадии (i) торрефикации материал биомассы нагревают до температуры от 320°С до 350°С.
6. Способ по пп.1, 2 или 5, в котором время пребывания материала биомассы в реакторе с тороидальным слоем на стадии (i) не превышает 5 мин.
7. Способ по п.6, в котором время пребывания материала биомассы в реакторе с тороидальным слоем на стадии (i) не превышает 60 с.
8. Способ по пп.1, 2, 5 или 7, в котором поток текучей среды внутри реакционной камеры имеет горизонтальную и вертикальную составляющие скорости.
9. Способ по пп.1, 2, 5 или 7, в котором камера имеет множество наклонных отходящих наружу впускных отверстий для текучей среды в основании камеры или возле него, причем текучая среда направляется через впускные отверстия в основании камеры для формирования внутри нее кругового потока текучей среды.
10. Способ по пп.1, 2, 5 или 7, в котором потоку, направляемому через указанные впускные отверстия, придается как горизонтальная, так и вертикальная компоненты скорости.
11. Способ по пп.1, 2, 5 или 7, включающий стадию удаления летучих компонентов путем нагрева материала биомассы до температуры в диапазоне от 200°С до 280°С перед осуществлением стадии (i).
12. Способ по пп.1, 2, 5 или 7, в котором материал биомассы подвергают по меньшей мере одной операции предварительной обработки, выбранной из сортировки, измельчения, просеивания и смешивания.
13. Способ по пп.1, 2, 5 или 7, в котором перед использованием материал биомассы подсушивают при температуре от 100°С до 200°С.
14. Способ по пп.1, 2, 5 или 7, в котором перед выполнением стадии (i) содержание воды в материале биомассы не превышает 20%.
15. Способ по п.14, в котором содержание воды не превышает 10%).
16. Способ по пп.1, 2, 5, 7 или 15, в котором на стадии (i), на дополнительной стадии подсушивания и/или дополнительной стадии удаления летучих компонентов из материала биомассы получают летучий газ, который сжигают для обеспечения по меньшей мере частичного тепла, необходимого на одной или нескольких стадиях способа.
17. Способ по пп.1, 2, 5, 7 или 15, в котором торрефикацию материала биомассы осуществляют в форме непрерывного процесса.
18. Способ по пп.1, 2, 5, 7 или 15, в котором выполняют завершающую стадию агломерирования для получения гранулированного или брикетированного биотоплива.
19. Способ по пп.1, 2, 5, 7 или 15, в котором способ включает также стадию смешивания торрефицированной биомассы с углем, причем количество угля предпочтительно находится в диапазоне от 90 вес.% до 75 вес.%.
20. Биотопливо, получаемое в соответствии со способом по любому из предыдущих пунктов.
21. Биотопливо, содержащее от 10 вес.% до 25 вес.% биотоплива, получаемого в соответствии со способом по любому из предыдущих пп.1-18, и уголь, составляющий остальную часть.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1007192A GB2479924A (en) | 2010-04-29 | 2010-04-29 | Torrefaction Process |
GB1007192.6 | 2010-04-29 | ||
PCT/GB2011/000660 WO2011135305A1 (en) | 2010-04-29 | 2011-04-28 | Torrefaction process |
Publications (1)
Publication Number | Publication Date |
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RU2012148762A true RU2012148762A (ru) | 2014-06-10 |
Family
ID=42271051
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2012148762/04A RU2012148762A (ru) | 2010-04-29 | 2011-04-28 | Способ торрефикации |
Country Status (7)
Country | Link |
---|---|
US (1) | US20130104450A1 (ru) |
EP (1) | EP2563885A1 (ru) |
BR (1) | BR112012027769A2 (ru) |
CA (1) | CA2797438A1 (ru) |
GB (1) | GB2479924A (ru) |
RU (1) | RU2012148762A (ru) |
WO (1) | WO2011135305A1 (ru) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2692250C2 (ru) * | 2015-01-23 | 2019-06-24 | Биоэндев Аб | Способ и система для торрефикации биомассы с низким потреблением энергии |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9487721B2 (en) * | 2011-03-25 | 2016-11-08 | Hm3 Energy, Inc. | Refined torrefied biomass |
WO2012145397A1 (en) | 2011-04-18 | 2012-10-26 | Hm3 Energy, Inc. | A system and process for producing torrefied biomass using a mass flow reactor |
US8198493B1 (en) | 2012-01-11 | 2012-06-12 | Earth Care Products, Inc. | High energy efficiency biomass conversion process |
FR2987434A1 (fr) * | 2012-02-28 | 2013-08-30 | Gexin Innovation | Procede et dispositif de conditionnement de matiere, notamment de dechets, sous forme de combustible solide |
US9683187B2 (en) | 2012-05-25 | 2017-06-20 | Airex Energie Inc. | Method and apparatus for torrefaction of biomass with a cyclonic bed reactor |
US9175235B2 (en) | 2012-11-15 | 2015-11-03 | University Of Georgia Research Foundation, Inc. | Torrefaction reduction of coke formation on catalysts used in esterification and cracking of biofuels from pyrolysed lignocellulosic feedstocks |
US9631156B2 (en) * | 2013-12-03 | 2017-04-25 | Clean Electricity Generation Uk Ltd | Torrefaction/gassification system |
EP2883943A1 (en) * | 2013-12-16 | 2015-06-17 | Arigna Fuels Limited | Manufacture of fuel briquettes from thermally processed biomass |
FR3017396B1 (fr) * | 2014-02-11 | 2017-07-07 | Jean-Paul Vieslet | Procede de transformation d’une biomasse en au moins un solide combustible |
AU2015256247B2 (en) * | 2014-05-05 | 2018-11-08 | Agri-Tech Producers, Llc | Combined remediation biomass and bio-product production process |
DE102014107969A1 (de) * | 2014-06-05 | 2015-12-17 | EnBW Energie Baden-Württemberg AG | Verfahren zur Behandlung einer feuchten, heizwertarmen Masse |
US20160298046A1 (en) * | 2014-06-16 | 2016-10-13 | Biomass Energy Enhancements Llc | Aggregates of Coal and Beneficiated Organic-Carbon-Containing Feedstock |
US20150361370A1 (en) * | 2014-06-16 | 2015-12-17 | Biomass Energy Enhancements Llc | Aggregates of Cleaned Low Energy Coal Fines and Beneficiated Organic-Carbon-Containng Feedstock |
US20160010016A1 (en) * | 2014-06-16 | 2016-01-14 | Biomass Energy Enhancements Llc | High Energy Aggregates of Coal Fines and Beneficiated Organic-Carbon-Containing Feedstock |
US20160010017A1 (en) * | 2014-06-16 | 2016-01-14 | Biomass Energy Enhancements Llc | Aggregates of Cleaned High Energy Coal Fines and Beneficiated Organic-Carbon-Containing Feedstock |
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RU2626852C1 (ru) * | 2016-03-31 | 2017-08-02 | Николай Иванович Акуленко | Способ торрефикации древесины |
FR3068708B1 (fr) * | 2017-07-07 | 2020-09-18 | Ifp Energies Now | Procede de traitement de la biomasse par co-broyage avec une charge fossile |
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US3977947A (en) * | 1972-07-26 | 1976-08-31 | The Kingsford Company | Fluidized bed carbonization |
US4070250A (en) * | 1976-06-25 | 1978-01-24 | Occidental Petroleum Corporation | Pyrolysis of carbonaceous materials in a double helix cyclone |
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GB2211597B (en) | 1987-10-23 | 1991-11-27 | Torftech Ltd | Processes in which matter is subjected to fluid flow |
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DK2291488T3 (da) * | 2008-06-25 | 2019-09-30 | Kior Inc | Fremgangsmåde til forbehandling af biomasse |
-
2010
- 2010-04-29 GB GB1007192A patent/GB2479924A/en not_active Withdrawn
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2011
- 2011-04-28 BR BR112012027769A patent/BR112012027769A2/pt not_active IP Right Cessation
- 2011-04-28 US US13/695,156 patent/US20130104450A1/en not_active Abandoned
- 2011-04-28 RU RU2012148762/04A patent/RU2012148762A/ru not_active Application Discontinuation
- 2011-04-28 EP EP11730389A patent/EP2563885A1/en not_active Withdrawn
- 2011-04-28 CA CA2797438A patent/CA2797438A1/en active Pending
- 2011-04-28 WO PCT/GB2011/000660 patent/WO2011135305A1/en active Application Filing
Cited By (1)
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RU2692250C2 (ru) * | 2015-01-23 | 2019-06-24 | Биоэндев Аб | Способ и система для торрефикации биомассы с низким потреблением энергии |
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BR112012027769A2 (pt) | 2017-08-08 |
GB201007192D0 (en) | 2010-06-09 |
US20130104450A1 (en) | 2013-05-02 |
WO2011135305A1 (en) | 2011-11-03 |
EP2563885A1 (en) | 2013-03-06 |
GB2479924A (en) | 2011-11-02 |
CA2797438A1 (en) | 2011-11-03 |
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