MX2009000384A - Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc. - Google Patents
Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc.Info
- Publication number
- MX2009000384A MX2009000384A MX2009000384A MX2009000384A MX2009000384A MX 2009000384 A MX2009000384 A MX 2009000384A MX 2009000384 A MX2009000384 A MX 2009000384A MX 2009000384 A MX2009000384 A MX 2009000384A MX 2009000384 A MX2009000384 A MX 2009000384A
- Authority
- MX
- Mexico
- Prior art keywords
- fcc unit
- catalyst
- naphtha
- downflow reactor
- paraffinic
- 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
- 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
- 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
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
-
- 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
- C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
- C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °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
- C10G2300/40—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)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
La producción de hidrocarburos ligeros que consisten de etileno, propileno, butilenos y de gasolina es aumentada mediante la introducción de una corriente de alimentación de nafta parafínica virgen derivada de una fuente externa hacia un reactor secundario de flujo descendente que utiliza la misma composición de catalizador que una unidad de FCC adyacente para fraccionar la nafta y extraer la corriente del producto de reacción de hidrocarburo más ligero deseado del reactor de flujo descendente y regenerar el catalizador en el mismo recipiente de regeneración que se usa para regenerar el catalizador gastado de la unidad de FCC. La eficiencia de la recuperación de los hidrocarburos olefínicos más ligeros deseados se maximiza limitando la corriente de alimentación al reactor de flujo descendente a nafta parafínica que puede ser procesada bajo condiciones relativamente más severas, mientras que se minimiza la producción de subproductos indeseados y se reduce la formación de coque en el catalizador.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/487,022 US20080011645A1 (en) | 2006-07-13 | 2006-07-13 | Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations |
PCT/US2007/016054 WO2008008527A2 (en) | 2006-07-13 | 2007-07-13 | Ancillary cracking of paraffinic naptha in conjunction with fcc unit operations |
Publications (2)
Publication Number | Publication Date |
---|---|
MX2009000384A true MX2009000384A (es) | 2009-04-06 |
MX345633B MX345633B (es) | 2017-02-08 |
Family
ID=38923953
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2009000384A MX345633B (es) | 2006-07-13 | 2007-07-13 | Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc. |
Country Status (11)
Country | Link |
---|---|
US (2) | US20080011645A1 (es) |
EP (1) | EP2052058A4 (es) |
JP (1) | JP5424879B2 (es) |
KR (1) | KR101526608B1 (es) |
CN (1) | CN101501164B (es) |
BR (1) | BRPI0713183B1 (es) |
CA (1) | CA2657628C (es) |
EA (1) | EA017596B1 (es) |
MX (1) | MX345633B (es) |
NO (1) | NO20090152L (es) |
WO (1) | WO2008008527A2 (es) |
Families Citing this family (47)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8137631B2 (en) * | 2008-12-11 | 2012-03-20 | Uop Llc | Unit, system and process for catalytic cracking |
US8889076B2 (en) | 2008-12-29 | 2014-11-18 | Uop Llc | Fluid catalytic cracking system and process |
EP2412786A4 (en) * | 2009-03-27 | 2012-10-17 | Chiyoda Corp | PROCESS FOR PRODUCING AROMATIC HYDROCARBON |
JP4837114B2 (ja) * | 2010-03-26 | 2011-12-14 | 千代田化工建設株式会社 | 芳香族炭化水素の製造方法および芳香族炭化水素の製造プラント |
TR201903230T4 (tr) | 2010-07-08 | 2019-03-21 | Indian Oil Corp Ltd | Çok aşamalı parçalama için fcc katalizörünün yukarı akış rejenerasyonu. |
US9458394B2 (en) | 2011-07-27 | 2016-10-04 | Saudi Arabian Oil Company | Fluidized catalytic cracking of paraffinic naphtha in a downflow reactor |
ES2652032T3 (es) | 2011-07-29 | 2018-01-31 | Saudi Arabian Oil Company | Procedimiento de hidrotratamiento selectivo de destilados medios |
WO2013142563A2 (en) * | 2012-03-20 | 2013-09-26 | Saudi Arabian Oil Company | Integrated hydroprocessing and fluid catalytic cracking for processing of a crude oil |
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 |
KR102201157B1 (ko) | 2012-10-19 | 2021-01-12 | 사우디 아라비안 오일 컴퍼니 | 원유의 고 강도 촉매 크래킹 공정 |
JP6560087B2 (ja) * | 2015-09-30 | 2019-08-14 | ルネサスエレクトロニクス株式会社 | 半導体装置および半導体装置の製造方法 |
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 |
US11208599B2 (en) | 2017-05-10 | 2021-12-28 | Sabic Global Technologies B.V. | Process for catalytic cracking of naphtha using radial flow moving bed reactor system |
US10870802B2 (en) | 2017-05-31 | 2020-12-22 | Saudi Arabian Oil Company | High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle |
US10781377B2 (en) * | 2017-11-30 | 2020-09-22 | Uop Llc | Process and apparatus for cracking hydrocarbons to lighter hydrocarbons |
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 |
US11905467B2 (en) | 2018-09-06 | 2024-02-20 | Sabic Global Technologies B.V. | Process for catalytic cracking of naphtha using multi-stage radial flow moving bed reactor system |
US11680521B2 (en) | 2019-12-03 | 2023-06-20 | Saudi Arabian Oil Company | Integrated production of hydrogen, petrochemicals, and power |
US11572517B2 (en) | 2019-12-03 | 2023-02-07 | Saudi Arabian Oil Company | Processing facility to produce hydrogen and petrochemicals |
US11193072B2 (en) | 2019-12-03 | 2021-12-07 | Saudi Arabian Oil Company | Processing facility to form 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 |
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 |
US11352575B2 (en) | 2020-09-01 | 2022-06-07 | Saudi Arabian Oil Company | Processes for producing petrochemical products that utilize hydrotreating of cycle oil |
US11505754B2 (en) | 2020-09-01 | 2022-11-22 | Saudi Arabian Oil Company | Processes for producing petrochemical products from atmospheric residues |
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 |
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 |
US11718522B2 (en) | 2021-01-04 | 2023-08-08 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via bi-reforming |
US11814289B2 (en) | 2021-01-04 | 2023-11-14 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via steam reforming |
US11427519B2 (en) | 2021-01-04 | 2022-08-30 | Saudi Arabian Oil Company | Acid modified red mud as a catalyst for olefin isomerization |
US11820658B2 (en) | 2021-01-04 | 2023-11-21 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via autothermal reforming |
US11724943B2 (en) | 2021-01-04 | 2023-08-15 | Saudi Arabian Oil Company | Black powder catalyst for hydrogen production via dry reforming |
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 |
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 |
Family Cites Families (45)
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 |
US3784463A (en) * | 1970-10-02 | 1974-01-08 | Texaco Inc | Catalytic cracking of naphtha and gas oil |
US3776838A (en) * | 1970-10-02 | 1973-12-04 | Texaco Inc | Catalytic cracking of naphthas |
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 |
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 |
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 |
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 |
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 |
US5582712A (en) * | 1994-04-29 | 1996-12-10 | Uop | Downflow FCC reaction arrangement with upflow regeneration |
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 |
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 |
GB2403434B (en) * | 2002-04-26 | 2005-09-14 | China Petroleum & Chemical | A downflow catalytic cracking reactor and its application |
AU2003264147A1 (en) * | 2002-08-29 | 2004-03-19 | Albemarle Netherlands B.V. | Catalyst for the production of light olefins |
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 |
RU2399648C2 (ru) * | 2004-08-10 | 2010-09-20 | Шелл Интернэшнл Рисерч Маатсхаппий Б.В. | Способ для получения среднедистиллятного продукта и низших олефинов из углеводородного сырья и устройство для его осуществления |
-
2006
- 2006-07-13 US US11/487,022 patent/US20080011645A1/en not_active Abandoned
-
2007
- 2007-07-13 BR BRPI0713183A patent/BRPI0713183B1/pt not_active IP Right Cessation
- 2007-07-13 CN CN2007800265994A patent/CN101501164B/zh not_active Expired - Fee Related
- 2007-07-13 WO PCT/US2007/016054 patent/WO2008008527A2/en active Application Filing
- 2007-07-13 MX MX2009000384A patent/MX345633B/es active IP Right Grant
- 2007-07-13 CA CA2657628A patent/CA2657628C/en not_active Expired - Fee Related
- 2007-07-13 JP JP2009519558A patent/JP5424879B2/ja not_active Expired - Fee Related
- 2007-07-13 EA EA200900185A patent/EA017596B1/ru not_active IP Right Cessation
- 2007-07-13 KR KR1020097002916A patent/KR101526608B1/ko not_active IP Right Cessation
- 2007-07-13 EP EP07796864A patent/EP2052058A4/en not_active Ceased
-
2009
- 2009-01-12 NO NO20090152A patent/NO20090152L/no not_active Application Discontinuation
-
2011
- 2011-06-09 US US13/156,440 patent/US20110240520A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
CN101501164A (zh) | 2009-08-05 |
EA017596B1 (ru) | 2013-01-30 |
BRPI0713183B1 (pt) | 2017-03-07 |
CA2657628C (en) | 2015-11-10 |
CA2657628A1 (en) | 2008-01-17 |
JP2009543899A (ja) | 2009-12-10 |
MX345633B (es) | 2017-02-08 |
US20110240520A1 (en) | 2011-10-06 |
EP2052058A2 (en) | 2009-04-29 |
BRPI0713183A2 (pt) | 2012-04-17 |
NO20090152L (no) | 2009-04-02 |
KR101526608B1 (ko) | 2015-06-05 |
US20080011645A1 (en) | 2008-01-17 |
KR20090043514A (ko) | 2009-05-06 |
EP2052058A4 (en) | 2011-11-16 |
EA200900185A1 (ru) | 2009-06-30 |
WO2008008527A2 (en) | 2008-01-17 |
WO2008008527A3 (en) | 2008-04-24 |
JP5424879B2 (ja) | 2014-02-26 |
CN101501164B (zh) | 2013-08-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
MX2009000384A (es) | Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc. | |
MX2009000383A (es) | Craqueo secundario de aceites pesados en conjunto con operaciones de la unidad de fcc. | |
CN101492608B (zh) | 劣质汽油深度脱硫降烯烃的方法 | |
WO2009045978A3 (en) | Method of producing low sulfur, high octane gasoline | |
RU2009115871A (ru) | Способ абсорбционного извлечения легких олефинов, не содержащих диоксида углерода | |
CN102839011B (zh) | 一种吸附脱硫方法 | |
RU2014103010A (ru) | Способ проведения каталитического крекинга с использованием двух лифт-реакторов для получения среднего дистиллятора и низших олефинов | |
RU2009144146A (ru) | Установка и способ получения средних дистиллятов и низших олефинов из углеводородного сырья | |
TW200615256A (en) | Method of producing ethylene and propylene | |
WO2010014549A3 (en) | Process for producing middle distillate by alkylating c5+ isoparaffin and c5+ olefin | |
WO2001000750A1 (en) | Catalytic converting process for producing prolifically diesel oil and liquefied gas | |
CN105349179A (zh) | 重质石油烃催化裂解与轻质石油烃蒸汽裂解组合工艺 | |
JP6111084B2 (ja) | 接触分解装置および接触分解から得られるガソリンの選択的水素化工程を用いて重質供給原料を転換するための方法 | |
CN101074392B (zh) | 一种利用两段催化裂解生产丙烯和高品质汽柴油的方法 | |
MY145121A (en) | A process for producing ethylene from ehanol combining the catalytic conversion of hydrocarbons | |
CN103773432B (zh) | 一种汽油脱硫方法 | |
CN103773431A (zh) | 一种汽油脱硫方法 | |
RU2014103008A (ru) | Способ проведения каталитического крекинга с использованием двух лифт-реакторов для получения среднего дистиллята и низших олефинов | |
WO2011143306A3 (en) | Process for the conversion of lower alkanes to aromatic hydrocarbons | |
CN103864563A (zh) | 用煤基甲醇制丙烯的烃类尾油副产物制备芳烃的方法 | |
US20130267742A1 (en) | Nitrile containing hydrocarbon feedstock, process for making the same and use thereof | |
CN1262625C (zh) | 一种催化裂化方法以及用于该方法的装置 | |
CN104629790B (zh) | 一种下行式流化床反应器及应用 | |
CN101892067A (zh) | 一种促进重油催化裂解提高丙烯收率和选择性的方法 | |
CN1212372C (zh) | 一种利用c4馏分增产小分子烯烃的催化转化方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
HH | Correction or change in general | ||
FG | Grant or registration |