JP2009543898A5 - - Google Patents
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- Publication number
- JP2009543898A5 JP2009543898A5 JP2009519539A JP2009519539A JP2009543898A5 JP 2009543898 A5 JP2009543898 A5 JP 2009543898A5 JP 2009519539 A JP2009519539 A JP 2009519539A JP 2009519539 A JP2009519539 A JP 2009519539A JP 2009543898 A5 JP2009543898 A5 JP 2009543898A5
- Authority
- JP
- Japan
- Prior art keywords
- cracking
- fcc
- reaction
- catalyst
- present
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 description 9
- 239000003054 catalyst Substances 0.000 description 6
- 238000005336 cracking Methods 0.000 description 6
- 229930195733 hydrocarbon Natural products 0.000 description 6
- 150000002430 hydrocarbons Chemical class 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000007795 chemical reaction product Substances 0.000 description 5
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- -1 ethylene, propylene Chemical group 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000006227 byproduct Chemical group 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/487,011 US20080011644A1 (en) | 2006-07-13 | 2006-07-13 | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
| US11/487,011 | 2006-07-13 | ||
| PCT/US2007/015950 WO2008008470A2 (en) | 2006-07-13 | 2007-07-11 | Ancillary cracking of heavy oils in conjuction with fcc unit operations |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JP2009543898A JP2009543898A (ja) | 2009-12-10 |
| JP2009543898A5 true JP2009543898A5 (enExample) | 2013-05-09 |
| JP5436209B2 JP5436209B2 (ja) | 2014-03-05 |
Family
ID=38923918
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2009519539A Expired - Fee Related JP5436209B2 (ja) | 2006-07-13 | 2007-07-11 | 転換増強方法及び生成物流を生産する生産方法 |
Country Status (11)
| Country | Link |
|---|---|
| US (2) | US20080011644A1 (enExample) |
| EP (1) | EP2046919A4 (enExample) |
| JP (1) | JP5436209B2 (enExample) |
| KR (1) | KR101447299B1 (enExample) |
| CN (1) | CN101743292B (enExample) |
| BR (1) | BRPI0713238A2 (enExample) |
| CA (1) | CA2657615C (enExample) |
| EA (1) | EA014574B1 (enExample) |
| MX (1) | MX2009000383A (enExample) |
| NO (1) | NO20090153L (enExample) |
| WO (1) | WO2008008470A2 (enExample) |
Families Citing this family (44)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080011644A1 (en) * | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
| EP2591073B1 (en) | 2010-07-08 | 2019-07-03 | Indian Oil Corporation Ltd. | Two stage fluid catalytic cracking process |
| CN104903427B (zh) * | 2012-10-19 | 2018-01-02 | 沙特阿拉伯石油公司 | 高强度催化裂化原油的方法 |
| EA201691762A1 (ru) * | 2013-11-19 | 2016-12-30 | Шеврон Ю.Эс.Эй. Инк. | Способ получения средних дистиллятов и тяжелого вакуумного газойля, служащего сырьем флюид-каталитического крекинга |
| EP3077484B1 (en) * | 2013-12-02 | 2020-04-01 | Saudi Arabian Oil Company | Integrated solvent-deasphalting and fluid catalytic cracking process for light olefin production |
| CN106609151B (zh) * | 2015-10-21 | 2018-05-18 | 中国石油化工股份有限公司 | 一种生产低碳烯烃的方法 |
| CN106609146B (zh) * | 2015-10-21 | 2018-06-19 | 中国石油化工股份有限公司 | 一种调节费托合成油催化裂化热平衡的方法 |
| US10851316B2 (en) | 2017-01-04 | 2020-12-01 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| US10844296B2 (en) | 2017-01-04 | 2020-11-24 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
| US10767117B2 (en) | 2017-04-25 | 2020-09-08 | Saudi Arabian Oil Company | Enhanced light olefin yield via steam catalytic downer pyrolysis of hydrocarbon feedstock |
| US10870802B2 (en) | 2017-05-31 | 2020-12-22 | Saudi Arabian Oil Company | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle |
| US10889768B2 (en) | 2018-01-25 | 2021-01-12 | Saudi Arabian Oil Company | High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds |
| CN108485704B (zh) * | 2018-04-17 | 2020-04-28 | 中国石油大学(华东) | 原油毫秒分级气相催化裂解和加氢组合最大化制取化工原料工艺 |
| US11680521B2 (en) | 2019-12-03 | 2023-06-20 | Saudi Arabian Oil Company | Integrated production of hydrogen, petrochemicals, and power |
| US11193072B2 (en) | 2019-12-03 | 2021-12-07 | Saudi Arabian Oil Company | Processing facility to form hydrogen and petrochemicals |
| US11572517B2 (en) | 2019-12-03 | 2023-02-07 | Saudi Arabian Oil Company | Processing facility to produce hydrogen and petrochemicals |
| US11426708B2 (en) | 2020-03-02 | 2022-08-30 | King Abdullah University Of Science And Technology | Potassium-promoted red mud as a catalyst for forming hydrocarbons from carbon dioxide |
| US11279891B2 (en) | 2020-03-05 | 2022-03-22 | Saudi Arabian Oil Company | Systems and processes for direct crude oil upgrading to hydrogen and chemicals |
| US11492255B2 (en) | 2020-04-03 | 2022-11-08 | Saudi Arabian Oil Company | Steam methane reforming with steam regeneration |
| US11420915B2 (en) | 2020-06-11 | 2022-08-23 | Saudi Arabian Oil Company | Red mud as a catalyst for the isomerization of olefins |
| US11495814B2 (en) | 2020-06-17 | 2022-11-08 | Saudi Arabian Oil Company | Utilizing black powder for electrolytes for flow batteries |
| US12000056B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Tandem electrolysis cell |
| US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
| US11492254B2 (en) | 2020-06-18 | 2022-11-08 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
| US11999619B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Hydrogen production with membrane reactor |
| US11434432B2 (en) | 2020-09-01 | 2022-09-06 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of a greater boiling point fraction with steam |
| US11230673B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of a lesser boiling point fraction with steam |
| US11242493B1 (en) | 2020-09-01 | 2022-02-08 | Saudi Arabian Oil Company | Methods for processing crude oils to form light olefins |
| US11230672B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking |
| US11332680B2 (en) | 2020-09-01 | 2022-05-17 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking of lesser and greater boiling point fractions with steam |
| US11505754B2 (en) | 2020-09-01 | 2022-11-22 | Saudi Arabian Oil Company | Processes for producing petrochemical products from atmospheric residues |
| US11352575B2 (en) | 2020-09-01 | 2022-06-07 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize hydrotreating of cycle oil |
| US11814289B2 (en) | 2021-01-04 | 2023-11-14 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via steam reforming |
| US11820658B2 (en) | 2021-01-04 | 2023-11-21 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via autothermal reforming |
| US11427519B2 (en) | 2021-01-04 | 2022-08-30 | Saudi Arabian Oil Company | Acid modified red mud as a catalyst for olefin isomerization |
| US11724943B2 (en) | 2021-01-04 | 2023-08-15 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via dry reforming |
| US11718522B2 (en) | 2021-01-04 | 2023-08-08 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via bi-reforming |
| US12258272B2 (en) | 2021-08-12 | 2025-03-25 | Saudi Arabian Oil Company | Dry reforming of methane using a nickel-based bi-metallic catalyst |
| US11578016B1 (en) | 2021-08-12 | 2023-02-14 | Saudi Arabian Oil Company | Olefin production via dry reforming and olefin synthesis in a vessel |
| US11787759B2 (en) | 2021-08-12 | 2023-10-17 | Saudi Arabian Oil Company | Dimethyl ether production via dry reforming and dimethyl ether synthesis in a vessel |
| US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol synthesis in a vessel |
| US12018392B2 (en) | 2022-01-03 | 2024-06-25 | Saudi Arabian Oil Company | Methods for producing syngas from H2S and CO2 in an electrochemical cell |
| US11617981B1 (en) | 2022-01-03 | 2023-04-04 | Saudi Arabian Oil Company | Method for capturing CO2 with assisted vapor compression |
| US12227704B2 (en) | 2022-11-03 | 2025-02-18 | Saudi Arabian Oil Company | Processes for producing petrochemical products from crude oil |
Family Cites Families (51)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3424672A (en) | 1967-01-09 | 1969-01-28 | Phillips Petroleum Co | Fluid catalytic stripping |
| US3542667A (en) | 1968-03-21 | 1970-11-24 | Foster Wheeler Corp | Process for the production of aromatic and olefinic hydrocarbons |
| US3617496A (en) * | 1969-06-25 | 1971-11-02 | Gulf Research Development Co | Fluid catalytic cracking process with a segregated feed charged to separate reactors |
| US3784463A (en) * | 1970-10-02 | 1974-01-08 | Texaco Inc | Catalytic cracking of naphtha and gas oil |
| US3856659A (en) * | 1972-12-19 | 1974-12-24 | Mobil Oil Corp | Multiple reactor fcc system relying upon a dual cracking catalyst composition |
| 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 |
| US4090949A (en) * | 1974-07-31 | 1978-05-23 | Mobil Oil Corportion | Upgrading of olefinic gasoline with hydrogen contributors |
| US4097363A (en) * | 1976-07-12 | 1978-06-27 | Gulf Research & Development Company | Thermal cracking of light gas oil at high severity to ethylene |
| US4116814A (en) * | 1977-07-18 | 1978-09-26 | Mobil Oil Corporation | Method and system for effecting catalytic cracking of high boiling hydrocarbons with fluid conversion catalysts |
| US4297203A (en) * | 1980-04-14 | 1981-10-27 | Standard Oil Company (Indiana) | Apparatus for the catalytic cracking of hydrocarbons |
| US4310489A (en) * | 1980-08-14 | 1982-01-12 | Standard Oil Company (Indiana) | Apparatus for the catalytic cracking of hydrocarbons |
| US4385985A (en) * | 1981-04-14 | 1983-05-31 | Mobil Oil Corporation | FCC Reactor with a downflow reactor riser |
| CA1237692A (en) | 1983-11-22 | 1988-06-07 | Shell Canada Limited | Dual riser fluid catalytic cracking process |
| US4693808A (en) * | 1986-06-16 | 1987-09-15 | Shell Oil Company | Downflow fluidized catalytic cranking reactor process and apparatus with quick catalyst separation means in the bottom thereof |
| 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 |
| US4814067A (en) * | 1987-08-11 | 1989-03-21 | Stone & Webster Engineering Corporation | Particulate solids cracking apparatus and process |
| US5049360A (en) * | 1988-01-19 | 1991-09-17 | Mobil Oil Corporation | Multi-stage conversion of alkanes to gasoline |
| US5053204A (en) * | 1988-12-30 | 1991-10-01 | Mobil Oil Corporation | Multiple feed point catalytic cracking apparatus using elutriable catalyst mixture |
| US5372704A (en) * | 1990-05-24 | 1994-12-13 | Mobil Oil Corporation | Cracking with spent catalyst |
| FR2667609B1 (fr) * | 1990-10-03 | 1993-07-16 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique en lit fluide a courant descendant. |
| US5314610A (en) * | 1992-05-29 | 1994-05-24 | Abb Lummus Crest Inc. | Staged catalytic cracking process |
| 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 |
| US5584986A (en) * | 1993-03-19 | 1996-12-17 | Bar-Co Processes Joint Venture | Fluidized process for improved stripping and/or cooling of particulate spent solids, and reduction of sulfur oxide emissions |
| CN2205827Y (zh) * | 1993-07-30 | 1995-08-23 | 北京联合应用化学与化学工程研究所 | 下行催化裂化提升管两段再生装置 |
| US5582712A (en) * | 1994-04-29 | 1996-12-10 | Uop | Downflow FCC reaction arrangement with upflow regeneration |
| JPH08322377A (ja) * | 1995-05-31 | 1996-12-10 | Nisshoku Corp | 建造物等の壁面緑化基体 |
| 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 |
| FR2753454B1 (fr) * | 1996-09-18 | 1999-06-04 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique descendant mettant en oeuvre l'injection d'une charge sous un angle adequat sur un catalyseur conditionne |
| 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 |
| US5846403A (en) * | 1996-12-17 | 1998-12-08 | Exxon Research And Engineering Company | Recracking of cat naphtha for maximizing light olefins yields |
| US6187272B1 (en) * | 1997-03-13 | 2001-02-13 | Nippon Mitsubishi Oil Corporation | Recycling fluidization system |
| JP3933745B2 (ja) * | 1997-03-14 | 2007-06-20 | 新日本石油株式会社 | 気固分離器 |
| US5965012A (en) * | 1997-12-05 | 1999-10-12 | Uop Llc | FCC process with short primary contacting and controlled secondary contacting |
| US6113776A (en) * | 1998-06-08 | 2000-09-05 | Uop Llc | FCC process with high temperature cracking zone |
| FR2785907B1 (fr) * | 1998-11-13 | 2001-01-05 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique comprenant des reacteurs a ecoulements descendant et ascendant |
| FR2802211B1 (fr) * | 1999-12-14 | 2002-02-01 | Inst Francais Du Petrole | Procede et dispositif de craquage catalytique comprenant en parallele au moins un reacteur a ecoulement ascendant et au moins un reacteur a ecoulement descendant |
| US20010042702A1 (en) * | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| 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 |
| US20020195373A1 (en) * | 2001-06-07 | 2002-12-26 | Takashi Ino | Heavy oil fluid catalytic cracking process |
| US6656346B2 (en) * | 2001-06-07 | 2003-12-02 | King Fahd University Of Petroleum And Minerals | Fluid catalytic cracking process for heavy oil |
| US6866771B2 (en) * | 2002-04-18 | 2005-03-15 | Uop Llc | Process and apparatus for upgrading FCC product with additional reactor with catalyst recycle |
| JP4456876B2 (ja) | 2002-04-26 | 2010-04-28 | 中国石油化工股▲分▼有限公司 | ダウンフロー接触分解反応器およびその応用 |
| KR100903898B1 (ko) * | 2002-08-29 | 2009-06-19 | 알베마를 네덜란드 비.브이. | 저급 올레핀 제조용 촉매 |
| US7087154B2 (en) * | 2002-12-30 | 2006-08-08 | Petroleo Brasileiro S.A. - Petrobras | Apparatus and process for downflow fluid catalytic cracking |
| US7144498B2 (en) * | 2004-01-30 | 2006-12-05 | Kellogg Brown & Root Llc | Supercritical hydrocarbon conversion process |
| WO2005080531A1 (en) * | 2004-02-10 | 2005-09-01 | Petroleo Brasileiro S.A. - Petrobras | Apparatus and process for downflow fluid catalytic cracking |
| AU2005274030B2 (en) | 2004-08-10 | 2008-11-20 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| US20080011644A1 (en) | 2006-07-13 | 2008-01-17 | Dean Christopher F | Ancillary cracking of heavy oils in conjuction with FCC unit operations |
-
2006
- 2006-07-13 US US11/487,011 patent/US20080011644A1/en not_active Abandoned
-
2007
- 2007-07-11 MX MX2009000383A patent/MX2009000383A/es active IP Right Grant
- 2007-07-11 CA CA2657615A patent/CA2657615C/en not_active Expired - Fee Related
- 2007-07-11 JP JP2009519539A patent/JP5436209B2/ja not_active Expired - Fee Related
- 2007-07-11 KR KR1020097002699A patent/KR101447299B1/ko not_active Expired - Fee Related
- 2007-07-11 CN CN200780026613.0A patent/CN101743292B/zh not_active Expired - Fee Related
- 2007-07-11 EA EA200900186A patent/EA014574B1/ru not_active IP Right Cessation
- 2007-07-11 WO PCT/US2007/015950 patent/WO2008008470A2/en not_active Ceased
- 2007-07-11 BR BRPI0713238-7A2A patent/BRPI0713238A2/pt not_active Application Discontinuation
- 2007-07-11 EP EP07796837A patent/EP2046919A4/en not_active Ceased
-
2009
- 2009-01-12 NO NO20090153A patent/NO20090153L/no not_active Application Discontinuation
-
2011
- 2011-05-19 US US13/111,437 patent/US8877042B2/en active Active
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