BRPI0514218A - processo e aparelho para fabricar destilado médio e olefinas inferiores - Google Patents
processo e aparelho para fabricar destilado médio e olefinas inferioresInfo
- Publication number
- BRPI0514218A BRPI0514218A BRPI0514218-0A BRPI0514218A BRPI0514218A BR PI0514218 A BRPI0514218 A BR PI0514218A BR PI0514218 A BRPI0514218 A BR PI0514218A BR PI0514218 A BRPI0514218 A BR PI0514218A
- Authority
- BR
- Brazil
- Prior art keywords
- cracking catalyst
- regenerated
- cracking
- catalyst
- medium
- Prior art date
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1809—Controlling processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
- C10G11/04—Oxides
- C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
- C10G11/182—Regeneration
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/026—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only only catalytic cracking steps
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °C
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/80—Additives
- C10G2300/805—Water
- C10G2300/807—Steam
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/08—Jet fuel
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Crystallography & Structural Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
PROCESSO E APARELHO PARA FABRICAR DESTILADO MéDIO E OLEFINAS INFERIORES Descreve-se um processo para fabricar destilado médio e olefinas inferiores. O processo inclui craquear cataliticamente uma carga de alimentação de gasóleo dentro de uma zona de reator de coluna ascendente por contato sob condições de craqueamento catalítico apropriadas dentro da zona de reator de coluna ascendente a carga de alimentação de gasóleo com um catalisador de craqueamento seletivo para destilado médio que compreende sílica alumina amorfa e um zeólito para produzir um produto de gasóleo craqueado e um catalisador de craqueamento gasto. O catalisador de craqueamento gasto é regenerado para produzir um catalisador de craqueamento regenerado. Dentro de uma zona de reator de leito denso e sob condições de craqueamento de severidade elevada apropriadas, uma carga de alimentação de gasolina é contatada com o catalisador de craqueamento regenerado para produzir um produto de gasolina craqueado e um catalisador de craqueamento regenerado usado. O catalisador de craqueanento regenerado usado é usado como o catalisador seletivo para destilado médio.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US60026404P | 2004-08-10 | 2004-08-10 | |
PCT/US2005/028053 WO2006020547A1 (en) | 2004-08-10 | 2005-08-08 | Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
Publications (1)
Publication Number | Publication Date |
---|---|
BRPI0514218A true BRPI0514218A (pt) | 2008-06-03 |
Family
ID=35106982
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BRPI0514218-0A BRPI0514218A (pt) | 2004-08-10 | 2005-08-08 | processo e aparelho para fabricar destilado médio e olefinas inferiores |
Country Status (11)
Country | Link |
---|---|
US (2) | US20060231461A1 (pt) |
EP (1) | EP1781759A1 (pt) |
JP (1) | JP2008510032A (pt) |
KR (1) | KR20070056090A (pt) |
CN (1) | CN101001938B (pt) |
AR (1) | AR051277A1 (pt) |
AU (1) | AU2005274030B2 (pt) |
BR (1) | BRPI0514218A (pt) |
CA (1) | CA2576329A1 (pt) |
RU (1) | RU2399648C2 (pt) |
WO (1) | WO2006020547A1 (pt) |
Families Citing this family (47)
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US6742593B2 (en) | 2000-04-24 | 2004-06-01 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using heat transfer from a heat transfer fluid to heat the formation |
US7004247B2 (en) | 2001-04-24 | 2006-02-28 | Shell Oil Company | Conductor-in-conduit heat sources for in situ thermal processing of an oil shale formation |
NZ532091A (en) | 2001-10-24 | 2005-12-23 | Shell Int Research | In situ recovery from a hydrocarbon containing formation using barriers |
JP2008510032A (ja) * | 2004-08-10 | 2008-04-03 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 炭化水素供給原料から中間留分生成物及び低級オレフィンを製造する方法及び装置 |
AU2006306471B2 (en) | 2005-10-24 | 2010-11-25 | Shell Internationale Research Maatschapij B.V. | Cogeneration systems and processes for treating hydrocarbon containing formations |
CN101045881B (zh) * | 2006-03-31 | 2010-06-23 | 中国石油化工股份有限公司 | 一种催化转化装置 |
AU2007240367B2 (en) | 2006-04-21 | 2011-04-07 | Shell Internationale Research Maatschappij B.V. | High strength alloys |
US20080011645A1 (en) * | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations |
US20080011644A1 (en) | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
ES2303448B1 (es) * | 2006-08-01 | 2009-06-22 | Universidad Politecnica De Valencia | Craqueo catalitico de compuestos organicos utilizando la zeolita itq-33. |
JP5330999B2 (ja) | 2006-10-20 | 2013-10-30 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 流体によるタールサンド地層の複数部分中での炭化水素の移動 |
US9701914B2 (en) * | 2006-11-07 | 2017-07-11 | Saudi Arabian Oil Company | Advanced control of severe fluid catalytic cracking process for maximizing propylene production from petroleum feedstock |
US20090095657A1 (en) * | 2006-11-07 | 2009-04-16 | Saudi Arabian Oil Company | Automation and Control of Energy Efficient Fluid Catalytic Cracking Processes for Maximizing Value Added Products |
US9764314B2 (en) * | 2006-11-07 | 2017-09-19 | Saudi Arabian Oil Company | Control of fluid catalytic cracking process for minimizing additive usage in the desulfurization of petroleum feedstocks |
US20100076096A1 (en) * | 2007-02-06 | 2010-03-25 | Hans Peter Alexander Calis | Process for the preparation of alkylate and middle distillate |
CN101679880B (zh) * | 2007-04-13 | 2013-05-22 | 国际壳牌研究有限公司 | 用于由烃原料生产中间馏分油产物和低级烯烃的系统和方法 |
WO2008131171A1 (en) | 2007-04-20 | 2008-10-30 | Shell Oil Company | Parallel heater system for subsurface formations |
EP2142619A1 (en) * | 2007-04-30 | 2010-01-13 | Shell Internationale Research Maatschappij B.V. | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
CN101952394B (zh) * | 2007-10-10 | 2013-09-11 | 国际壳牌研究有限公司 | 由烃原料制备中间馏分产物和低级烯烃的系统和方法 |
CA2700732A1 (en) | 2007-10-19 | 2009-04-23 | Shell Internationale Research Maatschappij B.V. | Cryogenic treatment of gas |
KR100904297B1 (ko) * | 2007-10-26 | 2009-06-25 | 한국화학연구원 | 연속적인 2단계 촉매 반응을 이용한 합성가스로부터 경질올레핀의 제조방법 |
RU2010121906A (ru) * | 2007-10-31 | 2013-01-27 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Установки и способы для получения среднедистиллятного продукта и низших олефинов из углеводородного исходного сырья |
EP2231821A1 (en) * | 2007-11-29 | 2010-09-29 | Shell Internationale Research Maatschappij B.V. | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
CN101959589B (zh) | 2008-03-07 | 2013-09-18 | 国际壳牌研究有限公司 | 用于裂化烃进料的反应器组件 |
RU2497933C2 (ru) * | 2008-03-13 | 2013-11-10 | Чайна Петролеум & Кемикал Корпорейшн | Способ преобразования низкосортного исходного сырья в нефтяное топливо высокого качества |
US8151907B2 (en) | 2008-04-18 | 2012-04-10 | Shell Oil Company | Dual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations |
WO2011056691A2 (en) * | 2009-11-09 | 2011-05-12 | Uop Llc | Process and apparatus for recovering products from two reactors |
FR2953851B1 (fr) * | 2009-12-14 | 2012-12-21 | Total Raffinage Marketing | Procede de craquage catalytique avec maximisation des bases gazoles |
CA2795120C (en) * | 2010-03-31 | 2019-10-08 | Indian Oil Corporation Ltd | A process for simulataneous cracking of lighter and heavier hydrocarbon feed and system for the same |
FR2968010B1 (fr) * | 2010-11-25 | 2014-03-14 | Ifp Energies Now | Procede de conversion d'une charge lourde en distillat moyen |
US20130001131A1 (en) | 2011-06-30 | 2013-01-03 | Shell Oil Company | Dual riser catalytic cracking process for making middle distillate and lower olefins |
CN103732726A (zh) | 2011-06-30 | 2014-04-16 | 国际壳牌研究有限公司 | 用于制备中间馏分油和低级烯烃的双提升管催化裂化方法 |
CN103814114B (zh) | 2011-07-27 | 2018-04-24 | 沙特阿拉伯石油公司 | 在下流式反应器中流化催化裂化链烷烃族石脑油 |
US20130130889A1 (en) * | 2011-11-17 | 2013-05-23 | Stone & Webster Process Technology, Inc. | Process for maximum distillate production from fluid catalytic cracking units (fccu) |
US20130178672A1 (en) | 2012-01-06 | 2013-07-11 | Shell Oil Company | Process for making a distillate product and/or c2-c4 olefins |
US9452404B2 (en) | 2012-07-12 | 2016-09-27 | Lummus Technology Inc. | Fluid cracking process and apparatus for maximizing light olefins or middle distillates and light olefins |
FR3019554B1 (fr) * | 2014-04-07 | 2017-10-27 | Ifp Energies Now | Procede de production d'olefines legeres et de btx utilisant une unite fcc traitant une charge lourde de type vgo tres hydrotraite, couplee avec une unite de reformage catalytique et un complexe aromatique traitant une charge de type naphta. |
TWI661867B (zh) * | 2014-10-14 | 2019-06-11 | 大陸商中國石油化工科技開發有限公司 | 流體化床反應器、反應再生設備和製備烯烴的方法以及製備芳烴的方法 |
JP7364467B2 (ja) | 2016-09-16 | 2023-10-18 | ラマス・テクノロジー・リミテッド・ライアビリティ・カンパニー | 軽質オレフィン収量を最大化するおよび他の適用のための流体接触分解プロセスおよび装置 |
US11396630B2 (en) * | 2016-12-13 | 2022-07-26 | Sabic Global Technologies B.V. | Naphtha catalytic cracking for light olefins production over cyclic regenerative process with dry gas diluent |
FR3068967B1 (fr) * | 2017-07-13 | 2019-06-28 | IFP Energies Nouvelles | Methode et procede pour convertir l'ethylene present dans l'effluent de tete d'un fcc de maniere a augmenter la production de propylene |
CN109519158A (zh) * | 2018-10-25 | 2019-03-26 | 安蔓页岩技术有限公司 | 一种一体开发含有机质的页岩和邻近的含油储层的方法 |
TW202104562A (zh) | 2019-04-03 | 2021-02-01 | 美商魯瑪斯科技有限責任公司 | 用於升級輕油系列材料之合併有固體分離裝置之分段流體化媒裂程序 |
CA3145743C (en) | 2019-07-02 | 2023-12-19 | Lummus Technology Llc | Fluid catalytic cracking processes and apparatus |
JP2022540497A (ja) | 2019-07-15 | 2022-09-15 | ラマス・テクノロジー・リミテッド・ライアビリティ・カンパニー | 軽質オレフィン収率の最大化および他の用途のための流動接触分解プロセスおよび装置 |
US11401475B2 (en) * | 2020-03-13 | 2022-08-02 | Lummus Technology Llc | Production of light olefins from crude oil via fluid catalytic cracking process and apparatus |
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-
2005
- 2005-08-08 JP JP2007525696A patent/JP2008510032A/ja not_active Abandoned
- 2005-08-08 CN CN2005800270546A patent/CN101001938B/zh not_active Expired - Fee Related
- 2005-08-08 BR BRPI0514218-0A patent/BRPI0514218A/pt not_active IP Right Cessation
- 2005-08-08 RU RU2007108775/04A patent/RU2399648C2/ru not_active IP Right Cessation
- 2005-08-08 KR KR1020077005551A patent/KR20070056090A/ko not_active Application Discontinuation
- 2005-08-08 WO PCT/US2005/028053 patent/WO2006020547A1/en active Application Filing
- 2005-08-08 AU AU2005274030A patent/AU2005274030B2/en not_active Ceased
- 2005-08-08 CA CA002576329A patent/CA2576329A1/en not_active Abandoned
- 2005-08-08 EP EP05783887A patent/EP1781759A1/en not_active Ceased
- 2005-08-08 US US11/199,050 patent/US20060231461A1/en not_active Abandoned
- 2005-08-09 AR ARP050103326A patent/AR051277A1/es unknown
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2006
- 2006-01-17 US US11/332,982 patent/US7632977B2/en active Active
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US20060178546A1 (en) | 2006-08-10 |
CN101001938B (zh) | 2012-01-11 |
KR20070056090A (ko) | 2007-05-31 |
CN101001938A (zh) | 2007-07-18 |
EP1781759A1 (en) | 2007-05-09 |
WO2006020547A1 (en) | 2006-02-23 |
AR051277A1 (es) | 2007-01-03 |
AU2005274030A1 (en) | 2006-02-23 |
RU2399648C2 (ru) | 2010-09-20 |
CA2576329A1 (en) | 2006-02-23 |
US20060231461A1 (en) | 2006-10-19 |
AU2005274030B2 (en) | 2008-11-20 |
US7632977B2 (en) | 2009-12-15 |
RU2007108775A (ru) | 2008-09-20 |
JP2008510032A (ja) | 2008-04-03 |
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