CL2007002877A1 - Proceso para producir nafta desde aceite pesado o bitumen usando una unidad fcc que comprende suministrar la alimentacion a la zona de reacion de la unidad con un catalizador en razon de peso catalizador/aceite entre 4 y 10 y y operar a n° de conversion entre 40 y 60; y sistema para producir mezcla de aceite pesado y nafta. - Google Patents

Proceso para producir nafta desde aceite pesado o bitumen usando una unidad fcc que comprende suministrar la alimentacion a la zona de reacion de la unidad con un catalizador en razon de peso catalizador/aceite entre 4 y 10 y y operar a n° de conversion entre 40 y 60; y sistema para producir mezcla de aceite pesado y nafta.

Info

Publication number
CL2007002877A1
CL2007002877A1 CL2007002877A CL2007002877A CL2007002877A1 CL 2007002877 A1 CL2007002877 A1 CL 2007002877A1 CL 2007002877 A CL2007002877 A CL 2007002877A CL 2007002877 A CL2007002877 A CL 2007002877A CL 2007002877 A1 CL2007002877 A1 CL 2007002877A1
Authority
CL
Chile
Prior art keywords
catalyst
heavy oil
gasoline
unit
oil
Prior art date
Application number
CL2007002877A
Other languages
English (en)
Inventor
Bruha Gerard
Original Assignee
Kellogg Brown & Root Llc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kellogg Brown & Root Llc filed Critical Kellogg Brown & Root Llc
Publication of CL2007002877A1 publication Critical patent/CL2007002877A1/es

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
    • C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
    • C10G67/0454—Solvent desasphalting
    • 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
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of catalytic cracking in the absence of hydrogen

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)

Abstract

Proceso para producir nafta de aceite pesado o bitumen usando unidad de craqueo catalítico fluidizado (fcc) que comprende suministrar alimentación a zona de reacción de unidad fcc con catalizador en razón de peso catalizador/aceite 4-10 y operar a n de conversión de 40-60; y aparato para producir mezcla de aceite pesado y nafta.
CL2007002877A 2006-10-09 2007-10-05 Proceso para producir nafta desde aceite pesado o bitumen usando una unidad fcc que comprende suministrar la alimentacion a la zona de reacion de la unidad con un catalizador en razon de peso catalizador/aceite entre 4 y 10 y y operar a n° de conversion entre 40 y 60; y sistema para producir mezcla de aceite pesado y nafta. CL2007002877A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US11/544,992 US7820034B2 (en) 2006-10-09 2006-10-09 Diluent from heavy oil upgrading

Publications (1)

Publication Number Publication Date
CL2007002877A1 true CL2007002877A1 (es) 2008-01-18

Family

ID=39283780

Family Applications (1)

Application Number Title Priority Date Filing Date
CL2007002877A CL2007002877A1 (es) 2006-10-09 2007-10-05 Proceso para producir nafta desde aceite pesado o bitumen usando una unidad fcc que comprende suministrar la alimentacion a la zona de reacion de la unidad con un catalizador en razon de peso catalizador/aceite entre 4 y 10 y y operar a n° de conversion entre 40 y 60; y sistema para producir mezcla de aceite pesado y nafta.

Country Status (3)

Country Link
US (1) US7820034B2 (es)
CL (1) CL2007002877A1 (es)
WO (1) WO2008045160A1 (es)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8602103B2 (en) * 2009-11-24 2013-12-10 Conocophillips Company Generation of fluid for hydrocarbon recovery
US20120084110A1 (en) * 2010-10-05 2012-04-05 M3 Technology, Inc. System and method for smart oil, gas and chemical process scheduling
US8877041B2 (en) * 2011-04-04 2014-11-04 Harris Corporation Hydrocarbon cracking antenna
US8911616B2 (en) 2011-04-26 2014-12-16 Uop Llc Hydrotreating process and controlling a temperature thereof
GB2505864B (en) * 2012-07-06 2019-04-24 Statoil Canada Ltd A method and system of recovering and processing a hydrocarbon mixture from a subterranean formation
MX366075B (es) 2014-08-27 2019-06-25 Mexicano Inst Petrol Proceso de mejoramiento parcial de crudos pesados y/o extra-pesados para su transporte.

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2879224A (en) * 1954-08-13 1959-03-24 Phillips Petroleum Co Separation of solids from fluids
US3647682A (en) 1968-10-23 1972-03-07 Union Carbide Corp Olefin production by the catalytic treatment of hydrocarbons
US3785782A (en) 1970-01-26 1974-01-15 Standard Oil Co Catalytic petroleum conversion apparatus
US3758403A (en) 1970-10-06 1973-09-11 Mobil Oil Olites catalytic cracking of hydrocarbons with mixture of zsm-5 and other ze
US4354923A (en) * 1979-11-14 1982-10-19 Ashland Oil, Inc. Carbo-metallic oil conversion with liquid water, ballistic separation and controlled CO:CO2 ratio during catalyst regeneration
US4419221A (en) 1981-10-27 1983-12-06 Texaco Inc. Cracking with short contact time and high temperatures
USRE33728E (en) 1981-11-24 1991-10-29 Total Engineering And Research Company Method for catalytically converting residual oils
US4404095A (en) 1982-07-22 1983-09-13 Mobil Oil Corporation Method and means for separating gaseous materials from finely divided catalyst particles
US4828679A (en) 1984-03-12 1989-05-09 Mobil Oil Corporation Octane improvement with large size ZSM-5 catalytic cracking
US4536283A (en) * 1984-08-20 1985-08-20 Exxon Research And Engineering Co. Integrated process for deasphalting heavy oils using a gaseous antisolvent
US4804459A (en) * 1985-04-04 1989-02-14 Engelhard Corporation Process for upgrading tar sand bitumen
US4875998A (en) 1986-11-07 1989-10-24 Solv-Ex Corporation Hot water bitumen extraction process
US4814067A (en) 1987-08-11 1989-03-21 Stone & Webster Engineering Corporation Particulate solids cracking apparatus and process
US4834865A (en) * 1988-02-26 1989-05-30 Amoco Corporation Hydrocracking process using disparate catalyst particle sizes
US5958365A (en) * 1998-06-25 1999-09-28 Atlantic Richfield Company Method of producing hydrogen from heavy crude oil using solvent deasphalting and partial oxidation methods
US6357526B1 (en) 2000-03-16 2002-03-19 Kellogg Brown & Root, Inc. Field upgrading of heavy oil and bitumen
US7097761B2 (en) * 2000-06-27 2006-08-29 Colt Engineering Corporation Method of removing water and contaminants from crude oil containing same
US6540023B2 (en) * 2001-03-27 2003-04-01 Exxonmobil Research And Engineering Company Process for producing a diesel fuel stock from bitumen and synthesis gas
US6773630B2 (en) * 2001-11-02 2004-08-10 Texaco Inc. Process for the gasification of heavy oil
US7381320B2 (en) 2004-08-30 2008-06-03 Kellogg Brown & Root Llc Heavy oil and bitumen upgrading

Also Published As

Publication number Publication date
US7820034B2 (en) 2010-10-26
US20080083653A1 (en) 2008-04-10
WO2008045160A1 (en) 2008-04-17

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