[go: up one dir, main page]

RU2006114599A - METHOD FOR PROCESSING CONDENSED FUEL BY GASIFICATION AND DEVICE FOR ITS IMPLEMENTATION - Google Patents

METHOD FOR PROCESSING CONDENSED FUEL BY GASIFICATION AND DEVICE FOR ITS IMPLEMENTATION

Info

Publication number
RU2006114599A
RU2006114599A RU2006114599/03A RU2006114599A RU2006114599A RU 2006114599 A RU2006114599 A RU 2006114599A RU 2006114599/03 A RU2006114599/03 A RU 2006114599/03A RU 2006114599 A RU2006114599 A RU 2006114599A RU 2006114599 A RU2006114599 A RU 2006114599A
Authority
RU
Russia
Prior art keywords
reactor
axis
fuel
zone
inclination
Prior art date
Application number
RU2006114599/03A
Other languages
Russian (ru)
Other versions
RU2322641C2 (en
Inventor
Сергей Олегович Дорофеенко (RU)
Сергей Олегович Дорофеенко
Андрей Юрьевич Зайченко (RU)
Андрей Юрьевич Зайченко
Александр Александрович Жирнов (RU)
Александр Александрович Жирнов
Георгий Борисович Манелис (RU)
Георгий Борисович Манелис
Евгений Викторович Полианчик (RU)
Евгений Викторович Полианчик
В чеслав Валентинович Черемисин (RU)
Вячеслав Валентинович Черемисин
Original Assignee
Некоммерческа организаци Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждени (ИПХФ РАН) (RU)
Некоммерческая организация Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждения (ИПХФ РАН)
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 Некоммерческа организаци Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждени (ИПХФ РАН) (RU), Некоммерческая организация Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждения (ИПХФ РАН) filed Critical Некоммерческа организаци Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждени (ИПХФ РАН) (RU)
Priority to RU2006114599/03A priority Critical patent/RU2322641C2/en
Priority to PL07747908T priority patent/PL2014744T3/en
Priority to CA002650979A priority patent/CA2650979A1/en
Priority to JP2009509473A priority patent/JP2009535478A/en
Priority to EP07747908.7A priority patent/EP2014744B1/en
Priority to PCT/RU2007/000200 priority patent/WO2007126335A1/en
Publication of RU2006114599A publication Critical patent/RU2006114599A/en
Application granted granted Critical
Publication of RU2322641C2 publication Critical patent/RU2322641C2/en
Priority to CY20161100130T priority patent/CY1117202T1/en

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/20—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having rotating or oscillating drums
    • 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
    • C10J3/005—Rotary drum or kiln gasifiers
    • 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
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C10J3/06—Continuous processes
    • C10J3/14—Continuous processes using gaseous heat-carriers
    • 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
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C10J3/20—Apparatus; Plants
    • C10J3/30—Fuel charging devices
    • 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
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C10J3/20—Apparatus; Plants
    • C10J3/32—Devices for distributing fuel evenly over the bed or for stirring up the fuel bed
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J1/00—Removing ash, clinker, or slag from combustion chambers
    • F23J1/02—Apparatus for removing ash, clinker, or slag from ash-pits, e.g. by employing trucks or conveyors, by employing suction devices
    • 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
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/09—Mechanical details of gasifiers not otherwise provided for, e.g. sealing means
    • 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
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C10J2200/156—Sluices, e.g. mechanical sluices for preventing escape of gas through the feed inlet
    • 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
    • C10J2300/1223—Heating the gasifier by burners
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/30—Pyrolysing
    • F23G2201/303—Burning pyrogases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/30—Pyrolysing
    • F23G2201/304—Burning pyrosolids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2205/00—Waste feed arrangements
    • F23G2205/18—Waste feed arrangements using airlock systems
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/52002—Rotary drum furnaces with counter-current flows of waste and gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
    • F23J2900/01007—Thermal treatments of ash, e.g. temper or shock-cooling for granulation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)

Claims (13)

1. Способ переработки конденсированного органического топлива путем газификации, включающий загрузку топлива в цилиндрический реактор, подачу в реактор газифицирующего агента, содержащего кислород, со стороны реактора, где происходит накопление твердых продуктов переработки, перемещение загруженного топлива вдоль оси реактора, вывод твердых продуктов переработки из реактора, вывод из реактора продуктов сушки, пиролиза и горения в виде продукт-газа, таким образом, что газификация проводится посредством последовательного пребывания топлива в зоне нагревания и сушки, зоне пиролиза, зоне горения (окисления) и зоне охлаждения, а газовый поток фильтруется через слой загруженного топлива, проходя последовательно зону охлаждения, зону горения, зону пиролиза и зону нагревания и сушки, отличающийся тем, что процесс горения в плотном слое стабилизируют, производя вращение реактора вокруг оси, наклонной по отношению к горизонту.1. A method of processing condensed fossil fuels by gasification, including loading fuel into a cylindrical reactor, feeding a gasification agent containing oxygen to the reactor from the side of the reactor, where solid processing products are accumulated, loaded fuel is moved along the axis of the reactor, and solid processing products are removed from the reactor conclusion from the reactor of products of drying, pyrolysis and combustion in the form of a product gas, so that gasification is carried out by successive stay t fuel in the heating and drying zone, the pyrolysis zone, the combustion (oxidation) zone and the cooling zone, and the gas stream is filtered through the loaded fuel layer, passing successively the cooling zone, the combustion zone, the pyrolysis zone and the heating and drying zone, characterized in that the combustion process in a dense layer they stabilize by rotating the reactor around an axis inclined with respect to the horizon. 2. Способ по п.1, отличающийся тем, что скорость вращения реактора вокруг оси выбирают из соотношения Т<D3/4V, где Т - период вращения (ч), D - диаметр проходного сечения реактора (м), V - объемная скорость выгрузки из реактора твердого остатка горения (м3/ч).2. The method according to claim 1, characterized in that the rotation speed of the reactor around the axis is selected from the ratio T <D 3 / 4V, where T is the rotation period (h), D is the diameter of the reactor cross section (m), V is the space velocity discharge from the reactor of solid combustion residue (m 3 / h). 3. Способ по п.1, отличающийся тем, что угол наклона оси реактора к горизонту поддерживают в пределах от 22 до 65°.3. The method according to claim 1, characterized in that the angle of inclination of the axis of the reactor to the horizon support in the range from 22 to 65 °. 4. Способ по п.3, отличающийся тем, что угол наклона реактора к горизонту поддерживают в пределах от 40 до 50°.4. The method according to claim 3, characterized in that the angle of inclination of the reactor to the horizon support in the range from 40 to 50 °. 5. Способ по п.1, отличающийся тем, что совместно с перерабатываемым топливом в реактор загружают твердый кусковой негорючий материал.5. The method according to claim 1, characterized in that, together with the processed fuel, solid lumpy non-combustible material is loaded into the reactor. 6. Способ по п.5, отличающийся тем, что в реактор загружают твердый кусковой негорючий материал с плотностью, отличающейся от плотности перерабатываемого топлива.6. The method according to claim 5, characterized in that a solid lump of non-combustible material with a density different from the density of the processed fuel is loaded into the reactor. 7. Устройство для переработки конденсированного топлива, включающее загрузочное устройство, цилиндрический реактор, разгрузочное устройство, устройство подачи газифицирующего агента, вывод продукт-газа, привод вращения реактора, уплотнения, обеспечивающие газоплотность реактора при вращении, отличающееся тем, что цилиндрический реактор установлен с углом наклона его оси к горизонту в пределах от 22 до 65°, причем загрузочное устройство и вывод продукт-газа расположены в верхней части реактора, а разгрузочное устройство и устройство подачи газифицирующего агента - в нижней части реактора.7. A device for processing condensed fuel, including a loading device, a cylindrical reactor, an unloading device, a gasifying agent supply device, a product gas outlet, a reactor rotation drive, and seals providing gas tightness of the reactor during rotation, characterized in that the cylindrical reactor is installed with an angle of inclination its axis to the horizon in the range from 22 to 65 °, with the loading device and product gas outlet located in the upper part of the reactor, and the unloading device and device under chi gasifying agent - in the lower part of the reactor. 8. Устройство по п.7, отличающееся тем, что угол наклона оси реактора к горизонту составляет от 40 до 50°.8. The device according to claim 7, characterized in that the angle of inclination of the axis of the reactor to the horizon is from 40 to 50 °. 9. Устройство по п.7, отличающееся тем, что в нижней части цилиндрической поверхности реактора имеется два или более отверстий с линейным размером не более половины внутреннего диаметра реактора.9. The device according to claim 7, characterized in that in the lower part of the cylindrical surface of the reactor there are two or more holes with a linear size of not more than half the inner diameter of the reactor. 10. Устройство по п.9, отличающееся тем, что отверстия на боковой поверхности реактора снабжены устройствами, изменяющими просвет отверстий, например, в виде регулируемых заслонок.10. The device according to claim 9, characterized in that the holes on the side surface of the reactor are equipped with devices that change the clearance of the holes, for example, in the form of adjustable dampers. 11. Устройство по п.7, отличающееся тем, что в нижней части цилиндрической поверхности реактора имеется конус, снабженный отверстием, расположенным на оси реактора, имеющим диаметр менее половины внутреннего диаметра реактора.11. The device according to claim 7, characterized in that in the lower part of the cylindrical surface of the reactor there is a cone equipped with a hole located on the axis of the reactor, having a diameter of less than half the inner diameter of the reactor. 12. Устройство по п.7, отличающееся тем, что длина реактора удовлетворяет условию L·sinα>3D, где L - длина реактора, α - угол наклона оси реактора к горизонту, а D - внутренний диаметр реактора.12. The device according to claim 7, characterized in that the length of the reactor satisfies the condition L · sinα> 3D, where L is the length of the reactor, α is the angle of inclination of the axis of the reactor to the horizontal, and D is the inner diameter of the reactor. 13. Устройство по п.7, отличающееся тем, что загрузочное устройство включает вертикальный цилиндр с диаметром меньше диаметра реактора, помещенный нижним концом внутрь верхней части реактора.13. The device according to claim 7, characterized in that the loading device includes a vertical cylinder with a diameter less than the diameter of the reactor, placed the lower end inside the upper part of the reactor.
RU2006114599/03A 2006-05-02 2006-05-02 Method and device for processing condensed fuel RU2322641C2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
RU2006114599/03A RU2322641C2 (en) 2006-05-02 2006-05-02 Method and device for processing condensed fuel
PL07747908T PL2014744T3 (en) 2006-05-02 2007-04-24 Method for processing condensed fuel by gasification and a device for carrying out said method
CA002650979A CA2650979A1 (en) 2006-05-02 2007-04-24 Method for processing condensed fuel by gasification and a device for carrying out said method
JP2009509473A JP2009535478A (en) 2006-05-02 2007-04-24 Method for treating condensed fuel by gasification and device for carrying out said method
EP07747908.7A EP2014744B1 (en) 2006-05-02 2007-04-24 Method for processing condensed fuel by gasification and a device for carrying out said method
PCT/RU2007/000200 WO2007126335A1 (en) 2006-05-02 2007-04-24 Method for processing condensed fuel by gasification and a device for carrying out said method
CY20161100130T CY1117202T1 (en) 2006-05-02 2016-02-16 METHOD FOR THE CONCENTRATED FUEL PROCESSING WITH AIR DISCHARGE AND APPLIANCE FOR THE IMPLEMENTATION OF THIS METHOD

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU2006114599/03A RU2322641C2 (en) 2006-05-02 2006-05-02 Method and device for processing condensed fuel

Publications (2)

Publication Number Publication Date
RU2006114599A true RU2006114599A (en) 2007-11-27
RU2322641C2 RU2322641C2 (en) 2008-04-20

Family

ID=38655776

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2006114599/03A RU2322641C2 (en) 2006-05-02 2006-05-02 Method and device for processing condensed fuel

Country Status (7)

Country Link
EP (1) EP2014744B1 (en)
JP (1) JP2009535478A (en)
CA (1) CA2650979A1 (en)
CY (1) CY1117202T1 (en)
PL (1) PL2014744T3 (en)
RU (1) RU2322641C2 (en)
WO (1) WO2007126335A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2376527C2 (en) * 2007-12-19 2009-12-20 Некоммерческая организация Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждения (ИПХФ РАН) Condensed fuel processing method and device for its implementation

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2496071C1 (en) * 2012-10-09 2013-10-20 Общество с ограниченной ответственностью "ЕВРОПРОФИЛЬ" (ООО "ЕВРОПРОФИЛЬ") Inclined rotary reactor
RU2518623C1 (en) * 2012-10-09 2014-06-10 Общество с ограниченной ответственностью "ЕВРОПРОФИЛЬ" (ООО "ЕВРОПРОФИЛЬ") Inclined rotating cylindrical reactor for loose materials processing
GB2527829A (en) * 2014-07-03 2016-01-06 Dps Bristol Holdings Ltd A gasifier
RU2584257C1 (en) * 2015-01-28 2016-05-20 Александр Вадимович Ивлев Method of processing condensed organic fuel by gasification
CN105018148B (en) * 2015-08-05 2017-10-03 中国东方电气集团有限公司 A kind of sleeve-type plasma gasification reacting furnace and its technique
RU2631812C2 (en) * 2015-12-28 2017-09-26 Федеральное государственное унитарное предприятие "Центр эксплуатации объектов наземной космической инфраструктуры" (ФГУП "ЦЭНКИ") Method of gasifying fuel biomass and device for its implementation
RU2631811C2 (en) * 2015-12-28 2017-09-26 Федеральное государственное унитарное предприятие "Центр эксплуатации объектов наземной космической инфраструктуры" (ФГУП "ЦЭНКИ") Method of gasifying fuel biomass and device for its implementation
RU2631808C2 (en) * 2015-12-28 2017-09-26 Федеральное государственное унитарное предприятие "Центр эксплуатации объектов наземной космической инфраструктуры" (ФГУП "ЦЭНКИ") Method of gasifying fuel biomass and device for its implementation
RU2663144C1 (en) * 2017-09-25 2018-08-01 Федеральное государственное унитарное предприятие "Центр эксплуатации объектов наземной космической инфраструктуры" (ФГУП "ЦЭНКИ") Method of gasification of solid fuel and device for its implementation
PL240502B1 (en) * 2018-01-23 2022-04-19 S E A Wagner Spolka Z Ograniczona Odpowiedzialnoscia Method for thermal utilization of municipal wastes and/or sewage sludges
EE05863B1 (en) * 2019-12-23 2024-01-15 Syngas OÜ Electrothermal reactor
NO346728B1 (en) * 2020-12-21 2022-12-05 Scanship As Char collector

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US247322A (en) 1881-09-20 Gas-retort
US1214164A (en) * 1916-06-24 1917-01-30 Gen Reduction Gas And By Products Company Process of treating materials.
US2796390A (en) 1952-01-31 1957-06-18 Socony Mobil Oil Co Inc Process of retorting of oil shale
US2798032A (en) 1953-02-26 1957-07-02 Carbonic Products Inc Method of destructively distilling oil shale in a producer-type of retort
US3990865A (en) 1974-10-21 1976-11-09 Allis-Chalmers Corporation Process for coal gasification utilizing a rotary kiln
US4374650A (en) * 1981-05-18 1983-02-22 Allis-Chalmers Corporation Bi-flow rotary kiln coal gasification process
US4378974A (en) * 1982-06-09 1983-04-05 Allis-Chalmers Corporation Start-up method for coal gasification plant
SU1291791A1 (en) * 1985-08-27 1987-02-23 Сибирский филиал Научно-производственного объединения "Техэнергохимпром" Rotary furnace
US4732091A (en) 1985-09-30 1988-03-22 G.G.C., Inc. Pyrolysis and combustion process and system
US5122189A (en) * 1990-04-13 1992-06-16 Hoke M. Garrett Manufacture of cement clinker in long rotary kilns by the addition of volatile fuels components directly into the calcining zone of the rotary kiln
RU2033588C1 (en) * 1991-04-29 1995-04-20 Институт газа АН Украины Plant for cleaning metal chips of organic impurities
RU2062284C1 (en) 1994-06-23 1996-06-20 Институт химической физики в Черноголовке РАН Method to process inflammable wastes like worn tires or similar rubber wastes
RU2079051C1 (en) 1994-06-23 1997-05-10 Институт химической физики в Черноголовке РАН Method of processing of solid domestic garbage
US5743196A (en) * 1996-09-03 1998-04-28 Beryozkin; Vladimir Mobile waste incinerator
RU2152561C1 (en) * 1998-01-22 2000-07-10 Институт проблем химической физики РАН Condensed combustibles recovery method
RU16193U1 (en) * 2000-06-15 2000-12-10 Двоскин Григорий Исакович WASTE PROCESSING PLANT
RU2167948C1 (en) * 2000-08-31 2001-05-27 Кашин Александр Викторович Metal and oil-containing wastes processing method and apparatus
US7220502B2 (en) * 2002-06-27 2007-05-22 Intellergy Corporation Process and system for converting carbonaceous feedstocks into energy without greenhouse gas emissions
US6932002B2 (en) * 2003-09-04 2005-08-23 Recycling Solutions Technology, Llc System and method of processing solid waste

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2376527C2 (en) * 2007-12-19 2009-12-20 Некоммерческая организация Учреждение Институт проблем химической физики Российской академии наук (статус государственного учреждения (ИПХФ РАН) Condensed fuel processing method and device for its implementation

Also Published As

Publication number Publication date
EP2014744A1 (en) 2009-01-14
CY1117202T1 (en) 2017-04-05
JP2009535478A (en) 2009-10-01
EP2014744A4 (en) 2012-04-11
EP2014744B1 (en) 2015-11-18
PL2014744T3 (en) 2016-04-29
WO2007126335A1 (en) 2007-11-08
RU2322641C2 (en) 2008-04-20
CA2650979A1 (en) 2007-11-08

Similar Documents

Publication Publication Date Title
RU2006114599A (en) METHOD FOR PROCESSING CONDENSED FUEL BY GASIFICATION AND DEVICE FOR ITS IMPLEMENTATION
BRPI0808815A2 (en) REDUCTION UNIT, SYSTEM FOR THERMOCHEMICAL CONVERSION OF FUEL MATERIAL, AND PROCESS FOR REDUCING TOTAL CURRENT AT LEAST PARTIALLY OXIDATED.
RU2010137001A (en) METHOD AND DEVICE FOR RECEIVING AND TRANSMISSION FROM SMALL TO LARGE-GRAIN SOLIDS FROM THE BUNKER TO THE PRESSURIZED SYSTEM
EA034879B1 (en) Co-current fixed-bed gasifier for producing a generator gas from pourable biomass particles
RU2721696C1 (en) Pyrolysis coke processing method to produce activated carbon by steam and gas activation
RU2012106201A (en) METHOD AND DEVICE FOR COOLING A FINE-GRAIN SOLID FILL WITH SIMULTANEOUS REPLACEMENT OF THE GAS CONTAINED IN THE VOLUME OF EMPTY
RU2007146624A (en) METHOD FOR PROCESSING CONDENSED FUEL AND DEVICE FOR ITS IMPLEMENTATION
KR102244255B1 (en) Reactor for producing a product gas from a fuel
EP2765177B1 (en) Gasification system
US3751214A (en) Method of and apparatus for conveying granular masses in tubular treating chambers
CA1134208A (en) Gasification furnace
RU2015156393A (en) METHOD FOR GASIFICATION OF FUEL BIOMASS AND DEVICE FOR ITS IMPLEMENTATION
US20030089038A1 (en) Pulverized coal pressurized gasifier system
FI70590B (en) PROCEDURE FOR THE FRAMEWORK OF FRAMSTAELLNING AV EN BRAENNBAR GASBLANDNING
US5580361A (en) Gas conditioner apparatus
US20060180459A1 (en) Gasifier
JP5355955B2 (en) Vertical firing furnace
RU2721695C1 (en) Method of processing organic material to produce synthetic fuel gas in a high-temperature ablation pyrolisis of gravitational type
RU2008137911A (en) METHOD OF HEAT AND MASS TRANSFER IN A VORTEX PRE-LIQUIDED LAYER AND A DEVICE FOR ITS IMPLEMENTATION
JP2023012957A (en) Manufacturing method of carbonized product and carbonization treatment equipment
JP6132584B2 (en) Raw material supply apparatus, drying equipment provided with the same, and raw material supply method
EP0955350A1 (en) A device and method for the gasification of wood
RU2797095C1 (en) Carbon waste recycling device using induction heating
RU209029U1 (en) Installation for the production of activated carbon from carbonaceous raw materials
JP2013257100A (en) Waste gasifying melting furnace

Legal Events

Date Code Title Description
MM4A The patent is invalid due to non-payment of fees

Effective date: 20100503

NF4A Reinstatement of patent

Effective date: 20110227

PD4A Correction of name of patent owner
QB4A Licence on use of patent

Free format text: LICENCE FORMERLY AGREED ON 20220208

Effective date: 20220208