BRPI0713238A2 - "método para intensificar a conversão de uma corrente de alimentação de óleo pesado e método para produzir uma corrente de porudto consistindo primariamente de olefinas leves" - Google Patents
"método para intensificar a conversão de uma corrente de alimentação de óleo pesado e método para produzir uma corrente de porudto consistindo primariamente de olefinas leves"Info
- Publication number
- BRPI0713238A2 BRPI0713238A2 BRPI0713238-7A2A BRPI0713238A BRPI0713238A2 BR PI0713238 A2 BRPI0713238 A2 BR PI0713238A2 BR PI0713238 A BRPI0713238 A BR PI0713238A BR PI0713238 A2 BRPI0713238 A2 BR PI0713238A2
- Authority
- BR
- Brazil
- Prior art keywords
- intensifying
- currently
- conversion
- producing
- heavy oil
- Prior art date
Links
Classifications
-
- 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
- C10G51/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel 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
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4006—Temperature
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4093—Catalyst stripping
-
- 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
- C10G2400/02—Gasoline
-
- 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)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (2)
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 |
PCT/US2007/015950 WO2008008470A2 (en) | 2006-07-13 | 2007-07-11 | Ancillary cracking of heavy oils in conjuction with fcc unit operations |
Publications (1)
Publication Number | Publication Date |
---|---|
BRPI0713238A2 true BRPI0713238A2 (pt) | 2014-10-29 |
Family
ID=38923918
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BRPI0713238-7A2A BRPI0713238A2 (pt) | 2006-07-13 | 2007-07-11 | "método para intensificar a conversão de uma corrente de alimentação de óleo pesado e método para produzir uma corrente de porudto consistindo primariamente de olefinas leves" |
Country Status (11)
Country | Link |
---|---|
US (2) | US20080011644A1 (pt) |
EP (1) | EP2046919A4 (pt) |
JP (1) | JP5436209B2 (pt) |
KR (1) | KR101447299B1 (pt) |
CN (1) | CN101743292B (pt) |
BR (1) | BRPI0713238A2 (pt) |
CA (1) | CA2657615C (pt) |
EA (1) | EA014574B1 (pt) |
MX (1) | MX2009000383A (pt) |
NO (1) | NO20090153L (pt) |
WO (1) | WO2008008470A2 (pt) |
Families Citing this family (42)
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 |
JP6262749B2 (ja) * | 2012-10-19 | 2018-01-17 | サウジ アラビアン オイル カンパニー | 原油の高過酷度接触分解方法 |
WO2015077152A1 (en) * | 2013-11-19 | 2015-05-28 | Chevron U.S.A. Inc. | Method for making middle distillates and a heavy vacuum gas oil fcc feedstock |
US20150152027A1 (en) * | 2013-12-02 | 2015-06-04 | Saudi Arabian Oil Company | Integrated solvent-deasphalting and fluid catalytic cracking process for light olefin production |
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 |
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 |
US10844296B2 (en) | 2017-01-04 | 2020-11-24 | Saudi Arabian Oil Company | Conversion of crude oil to aromatic and olefinic petrochemicals |
US10851316B2 (en) | 2017-01-04 | 2020-12-01 | 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 |
US11999619B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Hydrogen production with membrane reactor |
US11492254B2 (en) | 2020-06-18 | 2022-11-08 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
US11583824B2 (en) | 2020-06-18 | 2023-02-21 | Saudi Arabian Oil Company | Hydrogen production with membrane reformer |
US12000056B2 (en) | 2020-06-18 | 2024-06-04 | Saudi Arabian Oil Company | Tandem electrolysis cell |
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 |
US11230672B1 (en) | 2020-09-01 | 2022-01-25 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize fluid catalytic cracking |
US11352575B2 (en) | 2020-09-01 | 2022-06-07 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize hydrotreating of cycle oil |
US11242493B1 (en) | 2020-09-01 | 2022-02-08 | Saudi Arabian Oil Company | Methods for processing crude oils to form light olefins |
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 |
US11505754B2 (en) | 2020-09-01 | 2022-11-22 | Saudi Arabian Oil Company | Processes for producing petrochemical products from atmospheric residues |
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 |
US11724943B2 (en) | 2021-01-04 | 2023-08-15 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via dry reforming |
US11820658B2 (en) | 2021-01-04 | 2023-11-21 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via autothermal reforming |
US11814289B2 (en) | 2021-01-04 | 2023-11-14 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via steam reforming |
US11718522B2 (en) | 2021-01-04 | 2023-08-08 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via bi-reforming |
US11427519B2 (en) | 2021-01-04 | 2022-08-30 | Saudi Arabian Oil Company | Acid modified red mud as a catalyst for olefin isomerization |
US11718575B2 (en) | 2021-08-12 | 2023-08-08 | Saudi Arabian Oil Company | Methanol production via dry reforming and methanol synthesis in a vessel |
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 |
US11617981B1 (en) | 2022-01-03 | 2023-04-04 | Saudi Arabian Oil Company | Method for capturing CO2 with assisted vapor compression |
US12018392B2 (en) | 2022-01-03 | 2024-06-25 | Saudi Arabian Oil Company | Methods for producing syngas from H2S and CO2 in an electrochemical cell |
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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 |
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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 |
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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 |
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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 |
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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 |
US6656346B2 (en) * | 2001-06-07 | 2003-12-02 | King Fahd University Of Petroleum And Minerals | Fluid catalytic cracking process for heavy oil |
US20020195373A1 (en) * | 2001-06-07 | 2002-12-26 | Takashi Ino | Heavy oil fluid catalytic cracking process |
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 |
JP2005536343A (ja) * | 2002-08-29 | 2005-12-02 | アルベマーレ ネザーランズ ビー.ブイ. | 軽オレフィン生産のための触媒 |
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 |
CA2576329A1 (en) | 2004-08-10 | 2006-02-23 | 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 EA EA200900186A patent/EA014574B1/ru not_active IP Right Cessation
- 2007-07-11 MX MX2009000383A patent/MX2009000383A/es active IP Right Grant
- 2007-07-11 EP EP07796837A patent/EP2046919A4/en not_active Ceased
- 2007-07-11 WO PCT/US2007/015950 patent/WO2008008470A2/en active Application Filing
- 2007-07-11 KR KR1020097002699A patent/KR101447299B1/ko active IP Right Grant
- 2007-07-11 JP JP2009519539A patent/JP5436209B2/ja not_active Expired - Fee Related
- 2007-07-11 BR BRPI0713238-7A2A patent/BRPI0713238A2/pt not_active Application Discontinuation
- 2007-07-11 CN CN200780026613.0A patent/CN101743292B/zh not_active Expired - Fee Related
- 2007-07-11 CA CA2657615A patent/CA2657615C/en not_active Expired - Fee Related
-
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
Also Published As
Publication number | Publication date |
---|---|
US8877042B2 (en) | 2014-11-04 |
WO2008008470A3 (en) | 2008-03-13 |
CN101743292B (zh) | 2014-12-03 |
WO2008008470A2 (en) | 2008-01-17 |
CN101743292A (zh) | 2010-06-16 |
EA200900186A1 (ru) | 2009-10-30 |
EP2046919A4 (en) | 2012-09-05 |
NO20090153L (no) | 2009-04-02 |
KR101447299B1 (ko) | 2014-10-06 |
CA2657615C (en) | 2013-07-02 |
KR20090069266A (ko) | 2009-06-30 |
CA2657615A1 (en) | 2008-01-17 |
MX2009000383A (es) | 2009-08-18 |
WO2008008470A8 (en) | 2009-03-19 |
EP2046919A2 (en) | 2009-04-15 |
US20110226668A1 (en) | 2011-09-22 |
JP2009543898A (ja) | 2009-12-10 |
JP5436209B2 (ja) | 2014-03-05 |
EA014574B1 (ru) | 2010-12-30 |
US20080011644A1 (en) | 2008-01-17 |
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