RU2010118167A - METHOD FOR CARRYING OUT PYROLYSIS - Google Patents

METHOD FOR CARRYING OUT PYROLYSIS Download PDF

Info

Publication number
RU2010118167A
RU2010118167A RU2010118167/05A RU2010118167A RU2010118167A RU 2010118167 A RU2010118167 A RU 2010118167A RU 2010118167/05 A RU2010118167/05 A RU 2010118167/05A RU 2010118167 A RU2010118167 A RU 2010118167A RU 2010118167 A RU2010118167 A RU 2010118167A
Authority
RU
Russia
Prior art keywords
pyrolysis
stage
boiler
product
additional
Prior art date
Application number
RU2010118167/05A
Other languages
Russian (ru)
Other versions
RU2502779C2 (en
Inventor
Кай СИПИЛЯ (FI)
Кай СИПИЛЯ
Ирьё СОЛАНТАУСТА (FI)
Ирьё СОЛАНТАУСТА
Пекка ЙОКЕЛА (FI)
Пекка ЙОКЕЛА
Маркку РАЙКО (US)
Маркку РАЙКО
Original Assignee
Валтион Текниллинен Туткимускескус (Fi)
Валтион Текниллинен Туткимускескус
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 Валтион Текниллинен Туткимускескус (Fi), Валтион Текниллинен Туткимускескус filed Critical Валтион Текниллинен Туткимускескус (Fi)
Publication of RU2010118167A publication Critical patent/RU2010118167A/en
Application granted granted Critical
Publication of RU2502779C2 publication Critical patent/RU2502779C2/en

Links

Classifications

    • 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
    • C10B49/16—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 moving solid heat-carriers in divided form
    • C10B49/20—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 moving solid heat-carriers in divided form in dispersed form
    • C10B49/22—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 moving solid heat-carriers in divided form in dispersed form according to the "fluidised bed" technique
    • 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
    • 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
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/482—Gasifiers with stationary fluidised bed
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
    • C10J3/60—Processes
    • C10J3/64—Processes with decomposition of the distillation products
    • C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/001—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by thermal treatment
    • C10K3/003—Reducing the tar content
    • C10K3/006—Reducing the tar content by steam reforming
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0916—Biomass
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0956—Air or oxygen enriched air
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0983—Additives
    • C10J2300/0993—Inert particles, e.g. as heat exchange medium in a fluidized or moving bed, heat carriers, sand
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/12—Heating the gasifier
    • C10J2300/1246—Heating the gasifier by external or indirect heating
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1603—Integration of gasification processes with another plant or parts within the plant with gas treatment
    • C10J2300/1606—Combustion processes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1625—Integration of gasification processes with another plant or parts within the plant with solids treatment
    • C10J2300/1637—Char combustion
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/164—Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
    • C10J2300/1656—Conversion of synthesis gas to chemicals
    • C10J2300/1659—Conversion of synthesis gas to chemicals to liquid hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/164—Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
    • C10J2300/1656—Conversion of synthesis gas to chemicals
    • C10J2300/1665—Conversion of synthesis gas to chemicals to alcohols, e.g. methanol or ethanol
    • 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

1. Способ осуществления пиролиза, при котором первый исходный материал подают в котел для сжигания, а второй исходный материал подают в реактор пиролиза, которые объединены друг с другом; при этом в котле для сжигания из первого исходного материала получают энергию и передают ее из котла для сжигания в реактор пиролиза с помощью теплоносителя, теплоноситель нагревают в котле для сжигания, а в реакторе пиролиза из второго исходного материала получают газообразные и жидкие фракции продукта посредством быстрого пиролиза, отличающийся тем, что второй исходный материал смешивают с газом-носителем для получения смеси, а нагретый теплоноситель направляют в данную смесь, и получение фракций продукта пиролиза и энергии регулируют путем оптимизации выбора исходного материала, состава суммарного продукта и себестоимости производства, цены и качества по меньшей мере одной из фракций продукта посредством изменения технологических параметров, которые выбирают из группы, включающей первый исходный материал, второй исходный материал, количества исходных материалов, выбор дополнительных веществ, технологический режим, выбор дополнительной стадии процесса, состав и количество применяемого газа-носителя, количество кислорода, выбор теплоносителя и содержание влаги в исходном материале. ! 2. Способ по п.1, отличающийся тем, что газообразные фракции продукта, полученные во время пиролиза, главным образом, конденсируют в жидкие продукты пиролиза. ! 3. Способ по п.1, отличающийся тем, что исходный материал выбирают из группы, включающей органическое вещество, стружки, щепу лесоматериалов, древесину, кору, опилки, солому, угол 1. A method for carrying out pyrolysis, in which a first raw material is fed to a combustion boiler, and a second raw material is fed to a pyrolysis reactor, which are combined with each other; while in the combustion boiler, energy is obtained from the first source material and transferred from the combustion boiler to the pyrolysis reactor using a heat carrier, the heat carrier is heated in the combustion boiler, and in the pyrolysis reactor, gaseous and liquid product fractions are obtained from the second starting material by means of rapid pyrolysis characterized in that the second starting material is mixed with a carrier gas to obtain a mixture, and the heated heat carrier is directed into this mixture, and the production of pyrolysis product and energy fractions is controlled by optimizing the choice of the starting material, the composition of the total product and the production cost, price and quality at least one of the product fractions by changing technological parameters, which are selected from the group including the first starting material, the second starting material, the amount of starting materials, the choice of additional substances, the technological mode, the choice of an additional stage of the process, the composition and the amount of applied o carrier gas, amount of oxygen, choice of heat carrier and moisture content of the feed. ! 2. A method according to claim 1, characterized in that the gaseous product fractions obtained during pyrolysis are mainly condensed into liquid pyrolysis products. ! 3. The method according to claim 1, characterized in that the source material is selected from the group including organic matter, shavings, wood chips, wood, bark, sawdust, straw, angle

Claims (15)

1. Способ осуществления пиролиза, при котором первый исходный материал подают в котел для сжигания, а второй исходный материал подают в реактор пиролиза, которые объединены друг с другом; при этом в котле для сжигания из первого исходного материала получают энергию и передают ее из котла для сжигания в реактор пиролиза с помощью теплоносителя, теплоноситель нагревают в котле для сжигания, а в реакторе пиролиза из второго исходного материала получают газообразные и жидкие фракции продукта посредством быстрого пиролиза, отличающийся тем, что второй исходный материал смешивают с газом-носителем для получения смеси, а нагретый теплоноситель направляют в данную смесь, и получение фракций продукта пиролиза и энергии регулируют путем оптимизации выбора исходного материала, состава суммарного продукта и себестоимости производства, цены и качества по меньшей мере одной из фракций продукта посредством изменения технологических параметров, которые выбирают из группы, включающей первый исходный материал, второй исходный материал, количества исходных материалов, выбор дополнительных веществ, технологический режим, выбор дополнительной стадии процесса, состав и количество применяемого газа-носителя, количество кислорода, выбор теплоносителя и содержание влаги в исходном материале.1. The method of pyrolysis, in which the first source material is fed into the boiler for combustion, and the second source material is fed into the pyrolysis reactor, which are combined with each other; while in the boiler for burning from the first source material, energy is received and transferred from the boiler for burning to the pyrolysis reactor using a heat carrier, the heat carrier is heated in the boiler for burning, and in the pyrolysis reactor, gaseous and liquid fractions of the product are obtained by rapid pyrolysis characterized in that the second source material is mixed with a carrier gas to obtain a mixture, and the heated coolant is sent to this mixture, and the regulation of the production of pyrolysis product fractions and energy t by optimizing the selection of the starting material, the composition of the total product and the cost of production, price and quality of at least one of the product fractions by changing the technological parameters that are selected from the group including the first starting material, second starting material, the amount of starting materials, the choice of additional substances , technological mode, selection of an additional stage of the process, composition and amount of carrier gas used, amount of oxygen, choice of coolant and moisture content in the source material. 2. Способ по п.1, отличающийся тем, что газообразные фракции продукта, полученные во время пиролиза, главным образом, конденсируют в жидкие продукты пиролиза.2. The method according to claim 1, characterized in that the gaseous product fractions obtained during the pyrolysis are mainly condensed into liquid pyrolysis products. 3. Способ по п.1, отличающийся тем, что исходный материал выбирают из группы, включающей органическое вещество, стружки, щепу лесоматериалов, древесину, кору, опилки, солому, уголь, торф, масло, горючий сланец, бурый уголь, нефть, биомассу, энергосодержащие отходы, пластмассу, пластмассовые отходы, топливосодержащие отходы, топливо, полученное из отходов (ТПО), скипидар, черный щелок, органический растворитель и их производные.3. The method according to claim 1, characterized in that the source material is selected from the group comprising organic matter, shavings, wood chips, wood, bark, sawdust, straw, coal, peat, oil, oil shale, brown coal, oil, biomass , energy-containing waste, plastic, plastic waste, fuel-containing waste, fuel derived from waste (TPO), turpentine, black liquor, organic solvent and their derivatives. 4. Способ по п.1, отличающийся тем, что данный способ включает многостадийный пиролиз, где быстрый пиролиз осуществляют в качестве первой стадии, а фракции продукта с более высоким качеством и/или дополнительные фракции продукта получают во время второй стадии путем применения дополнительной стадии.4. The method according to claim 1, characterized in that the method includes multistage pyrolysis, where fast pyrolysis is carried out as a first stage, and higher quality product fractions and / or additional product fractions are obtained during the second stage by applying an additional stage. 5. Способ по п.1, отличающийся тем, что данный способ включает многостадийный пиролиз, где дополнительную стадию осуществляют в качестве первой стадии, а быстрый пиролиз осуществляют в качестве второй стадии, чтобы получить фракции продукта с более высоким качеством и/или дополнительные фракции продукта.5. The method according to claim 1, characterized in that the method includes multi-stage pyrolysis, where the additional stage is carried out as a first stage, and fast pyrolysis is carried out as a second stage, to obtain product fractions with higher quality and / or additional product fractions . 6. Способ по п.4, отличающийся тем, что дополнительную стадию выбирают из группы, включающей сушку, стадию повышения температуры, стадию газификации, отделение пыли, риформинг, паровой риформинг, разделение фракций продукта и отделение твердых веществ.6. The method according to claim 4, characterized in that the additional step is selected from the group consisting of drying, a step for raising the temperature, a gasification step, dust separation, reforming, steam reforming, product fraction separation and solids separation. 7. Способ по п.1, отличающийся тем, что осуществление стадии пиролиза модифицируют в данном способе посредством по меньшей мере одной особой операции, которую выбирают из группы, включающей регулирование температуры, выбор газа-носителя, подачу пара и добавление кислорода.7. The method according to claim 1, characterized in that the implementation of the pyrolysis stage is modified in this method by at least one special operation, which is selected from the group including temperature control, selection of a carrier gas, steam supply and the addition of oxygen. 8. Способ по п.1, отличающийся тем, что газ-носитель выбирают из группы, включающей газообразные продукты сгорания, водяной пар, воздух и их смесь.8. The method according to claim 1, characterized in that the carrier gas is selected from the group comprising gaseous products of combustion, water vapor, air and a mixture thereof. 9. Способ по п.1, отличающийся тем, что газ-носитель содержит кислород.9. The method according to claim 1, characterized in that the carrier gas contains oxygen. 10. Способ по п.1, отличающийся тем, что в газ-носитель добавляют дополнительный кислород.10. The method according to claim 1, characterized in that additional oxygen is added to the carrier gas. 11. Способ по п.1, отличающийся тем, что большинство потоков побочных продуктов, потоков остатков и потоков отходов направляют в котел для сжигания.11. The method according to claim 1, characterized in that most of the by-product streams, residue streams and waste streams are sent to a boiler for burning. 12. Способ по п.1, отличающийся тем, что для передачи энергии из котла для сжигания на требуемую стадию процесса и/или для регенерации энергии применяют теплоноситель.12. The method according to claim 1, characterized in that for the transfer of energy from the boiler for combustion to the desired stage of the process and / or for energy recovery, a coolant is used. 13. Способ по п.1, отличающийся тем, что теплоноситель выбирают из группы, включающей песок, пластовый песок, материал на основе оксида алюминия, другой материал для создания псевдоожиженного слоя и т.п.13. The method according to claim 1, characterized in that the coolant is selected from the group comprising sand, formation sand, alumina-based material, another material for creating a fluidized bed, and the like. 14. Способ по п.1, отличающийся тем, что теплоноситель прокачивают по замкнутой системе из котла для сжигания в реактор пиролиза и из реактора пиролиза в котел для сжигания через стадию разделения.14. The method according to claim 1, characterized in that the coolant is pumped through a closed system from the boiler for combustion to the pyrolysis reactor and from the pyrolysis reactor to the boiler for combustion through the separation stage. 15. Способ по любому из пп.1-14, отличающийся тем, что технологические параметры выбирают из группы, включающей температуру на стадии пиролиза, температуру на дополнительной стадии, время пребывания в реакторе пиролиза, температуру в котле для сжигания, способ смешивания и порядок смешивания исходных материалов для пиролиза, газа-носителя и теплоносителя, добавление кислорода, циркуляцию теплоносителя и циркуляцию продукта и побочных фракций. 15. The method according to any one of claims 1 to 14, characterized in that the technological parameters are selected from the group including the temperature in the pyrolysis stage, the temperature in the additional stage, the residence time in the pyrolysis reactor, the temperature in the combustion boiler, the mixing method and the mixing order starting materials for pyrolysis, carrier gas and coolant, the addition of oxygen, the circulation of the coolant and the circulation of the product and side fractions.
RU2010118167/05A 2007-10-11 2008-10-08 Method of conducting pyrolysis RU2502779C2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FI20075721A FI123455B (en) 2007-10-11 2007-10-11 Procedure for performing pyrolysis
US20075721 2007-10-11
PCT/FI2008/050558 WO2009047387A1 (en) 2007-10-11 2008-10-08 Method for carrying out pyrolysis

Publications (2)

Publication Number Publication Date
RU2010118167A true RU2010118167A (en) 2011-11-20
RU2502779C2 RU2502779C2 (en) 2013-12-27

Family

ID=38656868

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2010118167/05A RU2502779C2 (en) 2007-10-11 2008-10-08 Method of conducting pyrolysis

Country Status (8)

Country Link
US (1) US20110041388A1 (en)
EP (1) EP2209871A1 (en)
CN (1) CN101868516A (en)
BR (1) BRPI0817547A2 (en)
CA (1) CA2702193A1 (en)
FI (1) FI123455B (en)
RU (1) RU2502779C2 (en)
WO (1) WO2009047387A1 (en)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2647564C (en) 2006-04-03 2016-08-30 Pharmatherm Chemicals Inc. Thermal extraction method and product
US7905990B2 (en) 2007-11-20 2011-03-15 Ensyn Renewables, Inc. Rapid thermal conversion of biomass
WO2010137028A2 (en) * 2009-05-28 2010-12-02 Concord Blue Technology Pvt. Ltd. A process for generating energy from organic materials and/or biomass
FI125814B (en) 2009-06-02 2016-02-29 Valmet Technologies Oy Method for performing pyrolysis and pyrolysis apparatus
US8519203B2 (en) 2010-02-17 2013-08-27 Uop Llc Low oxygen biomass-derived pyrolysis oils and methods for producing the same
US20110284359A1 (en) 2010-05-20 2011-11-24 Uop Llc Processes for controlling afterburn in a reheater and for controlling loss of entrained solid particles in combustion product flue gas
US8499702B2 (en) 2010-07-15 2013-08-06 Ensyn Renewables, Inc. Char-handling processes in a pyrolysis system
US8519205B2 (en) 2010-07-23 2013-08-27 Ensyn Renewables, Inc. Low water biomass-derived pyrolysis oils and processes for producing the same
US20120061618A1 (en) * 2010-09-11 2012-03-15 James Santoianni Plasma gasification reactors with modified carbon beds and reduced coke requirements
US9441887B2 (en) 2011-02-22 2016-09-13 Ensyn Renewables, Inc. Heat removal and recovery in biomass pyrolysis
US9347005B2 (en) 2011-09-13 2016-05-24 Ensyn Renewables, Inc. Methods and apparatuses for rapid thermal processing of carbonaceous material
US10041667B2 (en) 2011-09-22 2018-08-07 Ensyn Renewables, Inc. Apparatuses for controlling heat for rapid thermal processing of carbonaceous material and methods for the same
US9044727B2 (en) 2011-09-22 2015-06-02 Ensyn Renewables, Inc. Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material
US10400175B2 (en) 2011-09-22 2019-09-03 Ensyn Renewables, Inc. Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material
US9109177B2 (en) 2011-12-12 2015-08-18 Ensyn Renewables, Inc. Systems and methods for renewable fuel
SG11201406590PA (en) * 2012-05-18 2014-11-27 Japan Blue Energy Co Ltd Biomass gasifier device
US9670413B2 (en) 2012-06-28 2017-06-06 Ensyn Renewables, Inc. Methods and apparatuses for thermally converting biomass
GB2503065B (en) 2013-02-20 2014-11-05 Recycling Technologies Ltd Process and apparatus for treating waste comprising mixed plastic waste
WO2014210150A1 (en) 2013-06-26 2014-12-31 Ensyn Renewables, Inc. Systems and methods for renewable fuel
CN104138886B (en) * 2014-06-30 2016-03-02 中国科学技术大学 A kind of method of fixed-contamination thing organophosphorus ester in copyrolysis process
DK3337966T3 (en) 2015-08-21 2022-02-28 Ensyn Renewables Inc HEATING SYSTEM WITH LIQUID BIOMASS
BR112019013387B1 (en) 2016-12-29 2023-03-28 Ensyn Renewables, Inc DEMETALIZATION OF BIOMASS
WO2021054897A1 (en) * 2019-09-17 2021-03-25 National University Of Singapore Waste treatment system
GB2618830A (en) * 2022-05-19 2023-11-22 Quantafuel Asa Processing of plastic

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3039955A (en) * 1958-08-21 1962-06-19 United Eng & Constructors Inc Pyrolysis process
US4064018A (en) * 1976-06-25 1977-12-20 Occidental Petroleum Corporation Internally circulating fast fluidized bed flash pyrolysis reactor
US4225392A (en) * 1978-09-05 1980-09-30 Taylor Leland T Pyrolysis apparatus
US4412910A (en) * 1981-10-21 1983-11-01 Westinghouse Electric Corp. Recovery of fuel from oil shale
US5136117A (en) * 1990-08-23 1992-08-04 Battelle Memorial Institute Monomeric recovery from polymeric materials
US6133499A (en) * 1996-02-29 2000-10-17 Mitsubishi Heavy Industries, Ltd. Method and apparatus for producing superheated steam using heat from the incineration of waste material
RU2125585C1 (en) * 1997-07-11 1999-01-27 Саратовский государственный технический университет Method of thermally processing slate
FI116902B (en) * 1998-10-14 2006-03-31 Valtion Teknillinen Method and apparatus for improving the quality of the pyrolysis liquid
FI117512B (en) * 1998-10-14 2006-11-15 Valtion Teknillinen Method and apparatus for producing pyrolysis oil
DE19945771C1 (en) * 1999-09-24 2001-02-22 Muehlen Gmbh & Co Kg Dr Process for gasifying organic materials comprises cracking the materials by contacting with a hot heat carrier medium which is removed from a solid carbonaceous residue after leaving the pyrolysis reactor and conveyed to a heating zone
FI120909B (en) * 2001-04-12 2010-04-30 Neste Oil Oyj A method for treating carbonaceous material
FI20030241A (en) * 2003-02-17 2004-08-18 Fortum Oyj A method for producing a synthesis gas
RU2240339C1 (en) * 2003-06-02 2004-11-20 Забарский Борис Лаврентьевич Installation for pyrolysis of hydrocarbonaceous raw material
RU2268910C2 (en) * 2003-10-28 2006-01-27 ОАО "Стройтрансгаз" Method of large-capacity production of a lump fuel charcoal and a device for its realization
CN101273114A (en) * 2005-04-29 2008-09-24 海塞特有限责任公司 System and method for conversion of hydrocarbon materials
FI122778B (en) * 2008-03-31 2012-06-29 Metso Power Oy Pyrolysis method in conjunction with a boiler, and pyrolysis device

Also Published As

Publication number Publication date
CN101868516A (en) 2010-10-20
BRPI0817547A2 (en) 2015-03-31
FI123455B (en) 2013-05-15
EP2209871A1 (en) 2010-07-28
WO2009047387A1 (en) 2009-04-16
FI20075721A0 (en) 2007-10-11
RU2502779C2 (en) 2013-12-27
US20110041388A1 (en) 2011-02-24
CA2702193A1 (en) 2009-04-16
FI20075721A (en) 2009-04-12

Similar Documents

Publication Publication Date Title
RU2010118167A (en) METHOD FOR CARRYING OUT PYROLYSIS
US9624109B2 (en) Method of manufacturing carbon-rich product and co-products
US8979952B2 (en) Method for the thermal treatment of biomass in connection with a boiler plant
CN101108970B (en) Method for manufacturing wet fuel by rapid common thermal decomposition of biomass and coal
RU2373263C2 (en) Method of transformation of solid bio-waste products into renewable fuel
RU2534085C2 (en) Lignocellulosic material roasting method and unit
FI123180B (en) Plant for the preparation of a pyrolysis product
CN102388119B (en) The manufacture method of biomass charcoal and the manufacturing installation for biomass charcoal wherein
US7029273B2 (en) Process for carbonizing wood residues and producing activated carbon
CN101787291B (en) High-efficiency and quick lignite pyrolysis method
NL2019552B1 (en) Process to prepare a char product and a syngas mixture
KR101279045B1 (en) Solid fuel using rice hull and dyeing sludge and manufacturing method thereof
RU2010109199A (en) FUEL, METHOD AND INSTALLATION FOR PRODUCING THERMAL ENERGY FROM BIOMASS
US10059883B2 (en) Method for producing a pyrolysis product
CA3135937A1 (en) Continuous reactor device and process for treatment of biomass
US20140283453A1 (en) Tyer carburetion process
WO2020093110A1 (en) Production of products from bio-energy
NL2019553B1 (en) Process to prepare an activated carbon product and a syngas mixture
JP2010254749A (en) Method for producing biomass charcoal and apparatus for producing biomass charcoal used in the same
WO2011076996A1 (en) Method for reducing greenhouse gas emissions in fuel applications of peat
CN115141657A (en) Method for preparing raw gas from biomass
Piętak et al. Possibilities of supplying internal combustion engines by wood gas
CZ200815A3 (en) Method of obtaining thermal energy from bioethanol stillage and apparatus for making the same

Legal Events

Date Code Title Description
PC41 Official registration of the transfer of exclusive right

Effective date: 20200907