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
- 238000000034 method Methods 0.000 title abstract 4
- 150000001336 alkenes Chemical class 0.000 title abstract 3
- 238000005336 cracking Methods 0.000 abstract 9
- 239000003054 catalyst Substances 0.000 abstract 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 2
- MXRIRQGCELJRSN-UHFFFAOYSA-N O.O.O.[Al] Chemical compound O.O.O.[Al] MXRIRQGCELJRSN-UHFFFAOYSA-N 0.000 abstract 1
- 229910021536 Zeolite Inorganic materials 0.000 abstract 1
- 238000004523 catalytic cracking Methods 0.000 abstract 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- 238000011144 upstream manufacturing Methods 0.000 abstract 1
- 239000010457 zeolite Substances 0.000 abstract 1
Classifications
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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 (48)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EA200201127A1 (ru) | 2000-04-24 | 2003-06-26 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Извлечение углеводородов на месте залегания из керогенсодержащей формации |
| US6877555B2 (en) | 2001-04-24 | 2005-04-12 | Shell Oil Company | In situ thermal processing of an oil shale formation while inhibiting coking |
| CN100540843C (zh) | 2001-10-24 | 2009-09-16 | 国际壳牌研究有限公司 | 利用自然分布型燃烧器对含烃岩层进行就地热处理的方法 |
| US20060231461A1 (en) * | 2004-08-10 | 2006-10-19 | Weijian Mo | Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| KR101434259B1 (ko) | 2005-10-24 | 2014-08-27 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | 탄화수소 함유 지층을 처리하기 위한 병합 발생 시스템 및방법 |
| 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 |
| EP2010754A4 (en) | 2006-04-21 | 2016-02-24 | Shell Int Research | ADJUSTING ALLOY COMPOSITIONS FOR SELECTED CHARACTERISTICS IN TEMPERATURE-LIMITED HEATERS |
| US20080011644A1 (en) | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
| US20080011645A1 (en) * | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of paraffinic naphtha 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. |
| CA2665865C (en) | 2006-10-20 | 2015-06-16 | Shell Internationale Research Maatschappij B.V. | Heating hydrocarbon containing formations in a spiral startup staged sequence |
| 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 |
| BRPI0718870A8 (pt) * | 2006-11-07 | 2017-02-07 | Saudi Arabian Oil Co | controle avançado de processo de craqueamento catalítico severo de fluido para maximizar a produção de propileno de uma matéria prima de petróleo |
| WO2008095882A1 (en) * | 2007-02-06 | 2008-08-14 | Shell Internationale Research Maatschappij B.V. | Process for the preparation of alkylate and middle distillate |
| US8920630B2 (en) | 2007-04-13 | 2014-12-30 | Shell Oil Company | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| CN101680287B (zh) | 2007-04-20 | 2013-12-18 | 国际壳牌研究有限公司 | 用于地下地层的加热系统和用于加热地下地层的方法 |
| RU2463335C2 (ru) * | 2007-04-30 | 2012-10-10 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Установка и способ получения средних дистиллятов и низших олефинов из углеводородного сырья |
| US20100324232A1 (en) * | 2007-10-10 | 2010-12-23 | Weijian Mo | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| JP5379804B2 (ja) | 2007-10-19 | 2013-12-25 | 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 | 炭化水素含有層の処理用熱源の不規則な間隔 |
| 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 |
| US20110034647A1 (en) * | 2007-11-29 | 2011-02-10 | Weijian Mo | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| WO2009109644A1 (en) | 2008-03-07 | 2009-09-11 | Shell Internationale Research Maatschappij B.V. | Process for cracking a hydrocarbon feed |
| US8597500B2 (en) * | 2008-03-13 | 2013-12-03 | China Petroleum & Chemical Corporation | Process for converting inferior feedstock to high quality fuel oil |
| EP2262978A1 (en) | 2008-04-18 | 2010-12-22 | Shell Internationale Research Maatschappij B.V. | Using mines and tunnels for treating subsurface hydrocarbon containing 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 |
| EP2726575A1 (en) | 2011-06-30 | 2014-05-07 | Shell Internationale Research Maatschappij B.V. | A dual riser catalytic cracking process for making middle distillate and lower olefins |
| US20130001130A1 (en) | 2011-06-30 | 2013-01-03 | Shell Oil Company | Dual riser catalytic cracking process for making middle distillate and lower olefins |
| 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 |
| WO2018053110A1 (en) | 2016-09-16 | 2018-03-22 | Lummus Technology Inc. | Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications |
| WO2018109639A1 (en) * | 2016-12-13 | 2018-06-21 | 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 |
| JP7239100B2 (ja) * | 2018-09-03 | 2023-03-14 | Eneos株式会社 | 炭素数6~8の単環芳香族炭化水素の製造方法 |
| 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 |
| TWI905097B (zh) | 2019-04-03 | 2025-11-21 | 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 |
| CN114080272B (zh) | 2019-07-02 | 2025-11-07 | 鲁姆斯科技有限责任公司 | 流化催化裂化方法和装置 |
| RS66533B1 (sr) | 2019-07-15 | 2025-03-31 | Lummus Technology Inc | Proces katalitičkog krekovanja fluida i uređaj za maksimalni prinos lakih olefina i druge primene |
| JP7601890B2 (ja) * | 2020-03-13 | 2024-12-17 | ルーマス テクノロジー エルエルシー | 流動接触分解プロセスによる原油からの軽質オレフィンの製造および装置 |
| US12391890B2 (en) * | 2020-09-01 | 2025-08-19 | Saudi Arabian Oil Company | Integrated process for conversion of whole crude to light olefins |
Family Cites Families (96)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US545313A (en) * | 1895-08-27 | Ronald j | ||
| US3130007A (en) * | 1961-05-12 | 1964-04-21 | Union Carbide Corp | Crystalline zeolite y |
| US3702886A (en) * | 1969-10-10 | 1972-11-14 | Mobil Oil Corp | Crystalline zeolite zsm-5 and method of preparing the same |
| US3709979A (en) * | 1970-04-23 | 1973-01-09 | Mobil Oil Corp | Crystalline zeolite zsm-11 |
| US3770614A (en) * | 1971-01-15 | 1973-11-06 | Mobil Oil Corp | Split feed reforming and n-paraffin elimination from low boiling reformate |
| US3832449A (en) * | 1971-03-18 | 1974-08-27 | Mobil Oil Corp | Crystalline zeolite zsm{14 12 |
| US3748251A (en) * | 1971-04-20 | 1973-07-24 | Mobil Oil Corp | Dual riser fluid catalytic cracking with zsm-5 zeolite |
| US3761391A (en) * | 1971-07-26 | 1973-09-25 | Universal Oil Prod Co | Process for the production of gasoline and low molecular weight hydrocarbons |
| US4051013A (en) * | 1973-05-21 | 1977-09-27 | Uop Inc. | Fluid catalytic cracking process for upgrading a gasoline-range feed |
| US3928172A (en) * | 1973-07-02 | 1975-12-23 | Mobil Oil Corp | Catalytic cracking of FCC gasoline and virgin naphtha |
| US4016245A (en) * | 1973-09-04 | 1977-04-05 | Mobil Oil Corporation | Crystalline zeolite and method of preparing same |
| US3894933A (en) * | 1974-04-02 | 1975-07-15 | Mobil Oil Corp | Method for producing light fuel oil |
| US3948758A (en) * | 1974-06-17 | 1976-04-06 | Mobil Oil Corporation | Production of alkyl aromatic hydrocarbons |
| US3974062A (en) * | 1974-10-17 | 1976-08-10 | Mobil Oil Corporation | Conversion of full range crude oils with low molecular weight carbon-hydrogen fragment contributors over zeolite catalysts |
| CA1064890A (en) * | 1975-06-10 | 1979-10-23 | Mae K. Rubin | Crystalline zeolite, synthesis and use thereof |
| GB1492880A (en) * | 1975-09-25 | 1977-11-23 | British Petroleum Co | Olefins production |
| NL7811732A (nl) * | 1978-11-30 | 1980-06-03 | Stamicarbon | Werkwijze voor de omzetting van dimethylether. |
| US4368114A (en) * | 1979-12-05 | 1983-01-11 | Mobil Oil Corporation | Octane and total yield improvement in catalytic cracking |
| US4310440A (en) * | 1980-07-07 | 1982-01-12 | Union Carbide Corporation | Crystalline metallophosphate compositions |
| US4309280A (en) * | 1980-07-18 | 1982-01-05 | Mobil Oil Corporation | Promotion of cracking catalyst octane yield performance |
| US4422925A (en) * | 1981-12-28 | 1983-12-27 | Texaco Inc. | Catalytic cracking |
| US4440871A (en) * | 1982-07-26 | 1984-04-03 | Union Carbide Corporation | Crystalline silicoaluminophosphates |
| US4500651A (en) * | 1983-03-31 | 1985-02-19 | Union Carbide Corporation | Titanium-containing molecular sieves |
| US4994173A (en) * | 1984-07-05 | 1991-02-19 | Mobil Oil Corporation | Method of adding zsm-5 containing catalyst to fluid bed catalytic cracking units |
| IN165201B (pt) | 1984-07-11 | 1989-08-26 | Mobil Oil Corp | |
| US4711710A (en) * | 1985-09-23 | 1987-12-08 | Mobil Oil Corporation | Process for making improved lubricating oils from heavy feedstock |
| US4686029A (en) | 1985-12-06 | 1987-08-11 | Union Carbide Corporation | Dewaxing catalysts and processes employing titanoaluminosilicate molecular sieves |
| US4731174A (en) * | 1986-04-28 | 1988-03-15 | Union Oil Company Of California | Process for cracking nitrogen-containing feedstocks |
| US4830728A (en) * | 1986-09-03 | 1989-05-16 | Mobil Oil Corporation | Upgrading naphtha in a multiple riser fluid catalytic cracking operation employing a catalyst mixture |
| US4803186A (en) * | 1986-12-04 | 1989-02-07 | Mobil Oil Corporation | Shape selective crystalline silicate zeolite containing intermetallic component and use as catalyst in hydrocarbon conversions |
| CN1004878B (zh) | 1987-08-08 | 1989-07-26 | 中国石油化工总公司 | 制取低碳烯烃的烃类催化转化方法 |
| US4830729A (en) * | 1987-12-28 | 1989-05-16 | Mobil Oil Corporation | Dewaxing over crystalline indium silicates containing groups VIII means |
| US4840928A (en) * | 1988-01-19 | 1989-06-20 | Mobil Oil Corporation | Conversion of alkanes to alkylenes in an external catalyst cooler for the regenerator of a FCC unit |
| US5234578A (en) * | 1988-08-26 | 1993-08-10 | Uop | Fluidized catalytic cracking process utilizing a high temperature reactor |
| US4927523A (en) * | 1988-12-12 | 1990-05-22 | Mobil Oil Corporation | Addition of shape selective zeolites to catalytic cracking units |
| US5055437A (en) * | 1988-12-30 | 1991-10-08 | Mobil Oil Corporation | Multi-component catalyst mixture and process for catalytic cracking of heavy hydrocarbon feed to lighter products |
| US4929337A (en) * | 1988-12-30 | 1990-05-29 | Mobil Oil Corporation | Process for catalytic cracking of heavy hydrocarbon feed to lighter products |
| US5009769A (en) | 1989-02-06 | 1991-04-23 | Stone & Webster Engineering Corporation | Process for catalytic cracking of hydrocarbons |
| US5168086A (en) * | 1989-03-02 | 1992-12-01 | W. R. Grace & Co.-Conn. | Catalytic cracking catalysis |
| US5000837A (en) * | 1989-04-17 | 1991-03-19 | Mobil Oil Corporation | Multistage integrated process for upgrading olefins |
| US4994995A (en) | 1990-03-14 | 1991-02-19 | International Business Machines Corporation | Bit-serial division method and apparatus |
| US5156817A (en) * | 1990-05-15 | 1992-10-20 | Exxon Research And Engineering Company | Fccu regenerator catalyst distribution system |
| US5372704A (en) * | 1990-05-24 | 1994-12-13 | Mobil Oil Corporation | Cracking with spent catalyst |
| GB9026775D0 (en) | 1990-12-10 | 1991-01-30 | Shell Int Research | Process for the preparation of an olefins-containing mixture of hydrocarbons |
| FR2675714B1 (fr) * | 1991-04-26 | 1993-07-16 | Inst Francais Du Petrole | Procede et dispositif d'echange thermique de particules solides pour regeneration en craquage catalytique. |
| US5234575A (en) * | 1991-07-31 | 1993-08-10 | Mobil Oil Corporation | Catalytic cracking process utilizing an iso-olefin enhancer catalyst additive |
| CN1089641A (zh) * | 1992-08-20 | 1994-07-20 | 史东及韦伯斯特工程公司 | 含高和低康拉逊残炭组分的富石蜡原料的催化裂化方法 |
| US5435906A (en) * | 1992-08-20 | 1995-07-25 | Stone & Webster Engineering Corporation | Process for catalytically cracking feedstocks paraffin rich comprising high and low concarbon components |
| US5318696A (en) * | 1992-12-11 | 1994-06-07 | Mobil Oil Corporation | Catalytic conversion with improved catalyst catalytic cracking with a catalyst comprising a large-pore molecular sieve component and a ZSM-5 component |
| US5346613A (en) * | 1993-09-24 | 1994-09-13 | Uop | FCC process with total catalyst blending |
| FI98529C (fi) * | 1994-03-31 | 1997-07-10 | Neste Oy | Menetelmä ja laitteisto keveiden olefiinien valmistamiseksi |
| US5521264A (en) * | 1995-03-03 | 1996-05-28 | Advanced Extraction Technologies, Inc. | Gas phase olefin polymerization process with recovery of monomers from reactor vent gas by absorption |
| JP3580518B2 (ja) | 1996-06-05 | 2004-10-27 | 新日本石油株式会社 | 重質油の流動接触分解法 |
| US5904837A (en) | 1996-10-07 | 1999-05-18 | Nippon Oil Co., Ltd. | Process for fluid catalytic cracking of oils |
| US6045690A (en) | 1996-11-15 | 2000-04-04 | Nippon Oil Co., Ltd. | Process for fluid catalytic cracking of heavy fraction oils |
| DE19648795A1 (de) * | 1996-11-26 | 1998-05-28 | Metallgesellschaft Ag | Verfahren zum Erzeugen von C¶3¶- und C¶4¶-Olefinen aus einem C¶4¶- bis C¶7¶-Olefine enthaltenden Einsatzgemisch |
| US5888378A (en) | 1997-03-18 | 1999-03-30 | Mobile Oil Corporation | Catalytic cracking process |
| IT1290433B1 (it) | 1997-03-24 | 1998-12-03 | Euron Spa | Processo di cracking catalitico a letto fluido caratterizzato da alta selettivita' ad olefine |
| JP3927704B2 (ja) | 1997-10-15 | 2007-06-13 | 中国石油化工集団公司 | 軽質オレフィンの生産のための接触式熱分解プロセスのための触媒およびその調製 |
| US5965012A (en) | 1997-12-05 | 1999-10-12 | Uop Llc | FCC process with short primary contacting and controlled secondary contacting |
| US6123832A (en) * | 1998-04-28 | 2000-09-26 | Exxon Research And Engineering Co. | Fluid catalytic cracking process for converting hydrocarbon mixtures |
| US6339180B1 (en) * | 1998-05-05 | 2002-01-15 | Exxonmobil Chemical Patents, Inc. | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
| US6106697A (en) * | 1998-05-05 | 2000-08-22 | Exxon Research And Engineering Company | Two stage fluid catalytic cracking process for selectively producing b. C.su2 to C4 olefins |
| US6455750B1 (en) * | 1998-05-05 | 2002-09-24 | Exxonmobil Chemical Patents Inc. | Process for selectively producing light olefins |
| US6123833A (en) * | 1998-09-22 | 2000-09-26 | Uop Llc | Method for controlling moisture in a catalyst regeneration process |
| US5944982A (en) * | 1998-10-05 | 1999-08-31 | Uop Llc | Method for high severity cracking |
| EP1049754A4 (en) | 1998-11-24 | 2002-04-17 | Exxonmobil Oil Corp | CATALYTIC CRACKING FOR THE PRODUCTION OF OLEFINS |
| US6656344B1 (en) * | 1998-12-23 | 2003-12-02 | Marri Rama Rao | Fluidized catalytic cracking process |
| US20020003103A1 (en) * | 1998-12-30 | 2002-01-10 | B. Erik Henry | Fluid cat cracking with high olefins prouduction |
| CA2372524C (en) * | 1999-05-11 | 2010-07-20 | Shell Internationale Research Maatschappij B.V. | Fluidized catalytic cracking process |
| US7169293B2 (en) * | 1999-08-20 | 2007-01-30 | Uop Llc | Controllable space velocity reactor and process |
| US6869521B2 (en) * | 2002-04-18 | 2005-03-22 | Uop Llc | Process and apparatus for upgrading FCC product with additional reactor with thorough mixing |
| US6166282A (en) * | 1999-08-20 | 2000-12-26 | Uop Llc | Fast-fluidized bed reactor for MTO process |
| DE10000889C2 (de) * | 2000-01-12 | 2002-12-19 | Mg Technologies Ag | Verfahren zum Erzeugen von C¶2¶- und C¶3¶-Olefinen aus Kohlenwasserstoffen |
| WO2001060951A1 (en) * | 2000-02-16 | 2001-08-23 | Indian Oil Corporation Limited | A multi stage selective catalytic cracking process and a system for producing high yield of middle distillate products from heavy hydrocarbon feedstocks |
| AU2001236985A1 (en) * | 2000-02-16 | 2001-08-27 | Exxonmobil Chemical Patents Inc | Treatment of molecular sieves with silicon containing compounds |
| US7102050B1 (en) * | 2000-05-04 | 2006-09-05 | Exxonmobil Chemical Patents Inc. | Multiple riser reactor |
| FR2811327B1 (fr) * | 2000-07-05 | 2002-10-25 | Total Raffinage Distribution | Procede et dispositif de craquage d'hydrocarbures mettant en oeuvre deux chambres reactionnelles successives |
| US6538169B1 (en) * | 2000-11-13 | 2003-03-25 | Uop Llc | FCC process with improved yield of light olefins |
| US6791022B2 (en) * | 2001-03-15 | 2004-09-14 | Philip Shepard Green | Stringed musical instrument |
| US6835302B2 (en) * | 2001-03-23 | 2004-12-28 | Uop Llc | FCC process and apparatus with automatic catalyst recycle control |
| JP4412886B2 (ja) * | 2001-08-29 | 2010-02-10 | 中國石油化工股▲分▼有限公司 | 石油炭化水素の接触分解処理 |
| EP1456325B1 (en) | 2001-12-21 | 2006-03-29 | Shell Internationale Researchmaatschappij B.V. | Process to regenerate spent fcc catalyst |
| US6866771B2 (en) * | 2002-04-18 | 2005-03-15 | Uop Llc | Process and apparatus for upgrading FCC product with additional reactor with catalyst recycle |
| DE10217866A1 (de) * | 2002-04-22 | 2003-11-06 | Linde Ag | Verfahren und Vorrichtung zur Olefinherstellung |
| US7122160B2 (en) * | 2002-09-24 | 2006-10-17 | Exxonmobil Chemical Patents Inc. | Reactor with multiple risers and consolidated transport |
| US7083762B2 (en) * | 2002-10-18 | 2006-08-01 | Exxonmobil Chemical Patents Inc. | Multiple riser reactor with centralized catalyst return |
| US20060283777A1 (en) * | 2002-10-29 | 2006-12-21 | Petroleo Brasileiro S.A. | Process for fluid catalytic cracking of hydrocarbon feedstocks with high levels of basic nitrogen |
| US6791002B1 (en) * | 2002-12-11 | 2004-09-14 | Uop Llc | Riser reactor system for hydrocarbon cracking |
| US7276149B2 (en) * | 2003-08-15 | 2007-10-02 | Exxonmobil Chemical Patents Inc. | Method of shutting down a reaction system |
| US7347930B2 (en) * | 2003-10-16 | 2008-03-25 | China Petroleum & Chemical Corporation | Process for cracking hydrocarbon oils |
| US20060231461A1 (en) * | 2004-08-10 | 2006-10-19 | Weijian Mo | Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| US7582203B2 (en) * | 2004-08-10 | 2009-09-01 | Shell Oil Company | Hydrocarbon cracking process for converting gas oil preferentially to middle distillate and lower olefins |
| FR2877671B1 (fr) * | 2004-11-09 | 2008-10-17 | Inst Francais Du Petrole | Dispositif et procede pour le craquage catalytique de deux charges distinctes d'hydrocarbures |
| US7288685B2 (en) * | 2005-05-19 | 2007-10-30 | Uop Llc | Production of olefins from biorenewable feedstocks |
| BRPI0502577B1 (pt) * | 2005-07-07 | 2015-11-03 | Petroleo Brasileiro Sa | processo de craqueamento catalítico para produção de diesel a partir de óleos vegetais |
-
2005
- 2005-08-08 US US11/199,050 patent/US20060231461A1/en not_active Abandoned
- 2005-08-08 JP JP2007525696A patent/JP2008510032A/ja not_active Abandoned
- 2005-08-08 BR BRPI0514218-0A patent/BRPI0514218A/pt not_active IP Right Cessation
- 2005-08-08 AU AU2005274030A patent/AU2005274030B2/en not_active Ceased
- 2005-08-08 EP EP05783887A patent/EP1781759A1/en not_active Ceased
- 2005-08-08 WO PCT/US2005/028053 patent/WO2006020547A1/en not_active Ceased
- 2005-08-08 CN CN2005800270546A patent/CN101001938B/zh not_active Expired - Fee Related
- 2005-08-08 KR KR1020077005551A patent/KR20070056090A/ko not_active Withdrawn
- 2005-08-08 RU RU2007108775/04A patent/RU2399648C2/ru not_active IP Right Cessation
- 2005-08-08 CA CA002576329A patent/CA2576329A1/en not_active Abandoned
- 2005-08-09 AR ARP050103326A patent/AR051277A1/es unknown
-
2006
- 2006-01-17 US US11/332,982 patent/US7632977B2/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| RU2007108775A (ru) | 2008-09-20 |
| KR20070056090A (ko) | 2007-05-31 |
| WO2006020547A1 (en) | 2006-02-23 |
| JP2008510032A (ja) | 2008-04-03 |
| AR051277A1 (es) | 2007-01-03 |
| AU2005274030B2 (en) | 2008-11-20 |
| RU2399648C2 (ru) | 2010-09-20 |
| CA2576329A1 (en) | 2006-02-23 |
| US20060178546A1 (en) | 2006-08-10 |
| EP1781759A1 (en) | 2007-05-09 |
| CN101001938B (zh) | 2012-01-11 |
| AU2005274030A1 (en) | 2006-02-23 |
| US7632977B2 (en) | 2009-12-15 |
| CN101001938A (zh) | 2007-07-18 |
| US20060231461A1 (en) | 2006-10-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| BRPI0514218A (pt) | processo e aparelho para fabricar destilado médio e olefinas inferiores | |
| KR102675222B1 (ko) | 석유계 물질을 처리하기 위한 수소화 처리 및 고-가혹도 유동화 촉매 분해를 포함한 시스템 및 방법 | |
| MX2009004863A (es) | Control avanzado de proceso severo de desintegracion catalitica de fluidos para maximizar la produccion de propileno a partir de materiales de alimentacion de petroleo. | |
| CN104560185B (zh) | 一种生产富含芳香族化合物汽油的催化转化方法 | |
| CO7250452A2 (es) | Proceso de craqueo catalítico fluido y aparato para miximizar olefinas ligeras o destilados medios y olefinas ligeras | |
| JP2015523345A5 (pt) | ||
| RU2009144146A (ru) | Установка и способ получения средних дистиллятов и низших олефинов из углеводородного сырья | |
| BR102018069324A2 (pt) | Processo de craqueamento catalítico com aumentada produção de uma gasolina tendo um baixo teor de olefina e um alto número de octanas | |
| HRP20211585T1 (hr) | Postupak pretvaranja velikog opterećenja pomoću jedinice za katalitički kreking i koraka za selektivnog hidrogeniranja benzina iz katalitičkog krekiranja | |
| CN104560187B (zh) | 一种生产富含芳烃汽油的催化转化方法 | |
| KR20220087536A (ko) | 저-탄소 올레핀 및 저-황 연료 오일 성분의 제조 방법 | |
| Doronin et al. | Advanced developments: Cracking catalysts and additives to them | |
| CN114437825B (zh) | 一种废塑料油和/或废旧轮胎油制备芳烃抽提原料的方法和系统 | |
| CN114437775A (zh) | 一种废塑料油和/或废旧轮胎油生产芳烃抽提原料的方法和系统 | |
| US20140323788A1 (en) | Process for modifying an apparatus and for removing one or more contaminants | |
| RU2443757C2 (ru) | Способ гидрообработки парафина и способ производства базового топлива | |
| CN1597864A (zh) | 一种劣质汽油加氢处理方法 | |
| CN104557378B (zh) | 一种石脑油催化裂解产丙烯的方法 | |
| CN104560186A (zh) | 一种最大化汽油生产的催化转化方法 | |
| CN1087023C (zh) | 一种馏分油非临氢降凝的方法 | |
| CN102911734B (zh) | 一种高硫蜡油的催化转化方法 | |
| CN102911731B (zh) | 一种高硫蜡油的催化转化方法 | |
| CN114437794A (zh) | 一种加工废塑料油和/或废旧轮胎油的方法和系统 | |
| JP6446434B2 (ja) | 水素化油の製造方法及び単環芳香族炭化水素の製造方法 | |
| CN104557400A (zh) | 一种石脑油催化裂解产丙烯的方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| B08F | Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette] |
Free format text: REFERENTE A 6A ANUIDADE. |
|
| B08K | Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette] |
Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 2158 DE 15/05/2012. |