FR2969650B1 - Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde - Google Patents

Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde

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Publication number
FR2969650B1
FR2969650B1 FR1061244A FR1061244A FR2969650B1 FR 2969650 B1 FR2969650 B1 FR 2969650B1 FR 1061244 A FR1061244 A FR 1061244A FR 1061244 A FR1061244 A FR 1061244A FR 2969650 B1 FR2969650 B1 FR 2969650B1
Authority
FR
France
Prior art keywords
liquid
schist
hydrocarbonate
hydroconversion
oil
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.)
Expired - Fee Related
Application number
FR1061244A
Other languages
English (en)
French (fr)
Other versions
FR2969650A1 (fr
Inventor
Christophe Halais
Helene Leroy
Frederic Morel
Cecile Plain
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Axens SA
Original Assignee
Axens SA
Total Raffinage Marketing SA
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
Priority to FR1061244A priority Critical patent/FR2969650B1/fr
Application filed by Axens SA, Total Raffinage Marketing SA filed Critical Axens SA
Priority to AU2011347041A priority patent/AU2011347041B2/en
Priority to PCT/FR2011/053020 priority patent/WO2012085406A1/fr
Priority to CN201180062209.5A priority patent/CN103339233B/zh
Priority to RU2013134382/04A priority patent/RU2592690C2/ru
Priority to US13/884,114 priority patent/US20130319911A1/en
Priority to CA2815618A priority patent/CA2815618C/fr
Priority to BR112013013951A priority patent/BR112013013951A2/pt
Priority to EEP201300023A priority patent/EE05762B1/et
Publication of FR2969650A1 publication Critical patent/FR2969650A1/fr
Priority to IL226639A priority patent/IL226639A/en
Priority to MA36029A priority patent/MA34751B1/fr
Application granted granted Critical
Publication of FR2969650B1 publication Critical patent/FR2969650B1/fr
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G67/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02Treatment 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
    • C10G67/04Treatment 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
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    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/002Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10G21/00Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/12Organic compounds only
    • C10G21/16Oxygen-containing compounds
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    • C10G21/00Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/12Organic compounds only
    • C10G21/27Organic compounds not provided for in a single one of groups C10G21/14 - C10G21/26
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    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
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    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
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    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12Inorganic carriers
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    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/24Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
    • C10G47/26Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles suspended in the oil, e.g. slurries
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    • C10G65/00Treatment of hydrocarbon oils by two or more hydrotreatment processes only
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    • C10G65/00Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
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    • C10G65/00Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/14Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only
    • C10G65/16Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only including only refining steps
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    • C10G67/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02Treatment 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
    • C10G67/04Treatment 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
    • C10G67/0409Extraction of unsaturated hydrocarbons
    • C10G67/0445The hydrotreatment being a hydrocracking
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    • C10G67/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
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    • C10G69/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/04Treatment 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
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    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/04Diesel oil

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  • General Chemical & Material Sciences (AREA)
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  • Wood Science & Technology (AREA)
  • Inorganic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
FR1061244A 2010-12-24 2010-12-24 Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde Expired - Fee Related FR2969650B1 (fr)

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Application Number Priority Date Filing Date Title
FR1061244A FR2969650B1 (fr) 2010-12-24 2010-12-24 Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde
EEP201300023A EE05762B1 (et) 2010-12-24 2011-12-16 Meetod põlevkiviõli sisaldava süsivesiniktoorme töötlemiseks, mis hõlmab hüdrogeenivat krakkimist keevkihis, fraktsioneerimist atmosfäärdestillatsioonil ja raske fraktsiooni vedelik-vedelik-ekstraktsiooni
CN201180062209.5A CN103339233B (zh) 2010-12-24 2011-12-16 通过在沸腾床中加氢转化、通过常压蒸馏分馏和重质馏分的液/液抽提的转化包含页岩油的烃原料的方法
RU2013134382/04A RU2592690C2 (ru) 2010-12-24 2011-12-16 Способ конверсии углеводородного сырья, содержащего сланцевое масло, путем гидроконверсии в кипящем слое, фракционирования с помощью атмосферной дистилляции и экстракции жидкость/жидкость в тяжелой фракции
US13/884,114 US20130319911A1 (en) 2010-12-24 2011-12-16 Method for converting hydrocarbon feedstock comprising a shale oil by hydroconversion in an ebullating bed, fractionation by atmospheric distillation and liquid/liquid extraction of the heavy fraction
CA2815618A CA2815618C (fr) 2010-12-24 2011-12-16 Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde
AU2011347041A AU2011347041B2 (en) 2010-12-24 2011-12-16 Method for converting hydrocarbon feedstock comprising a shale oil by hydroconversion in an ebullating bed, fractionation by atmospheric distillation and liquid/liquid extraction of the heavy fraction
PCT/FR2011/053020 WO2012085406A1 (fr) 2010-12-24 2011-12-16 Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde.
BR112013013951A BR112013013951A2 (pt) 2010-12-24 2011-12-16 processo de conversão de carga hidrocarbonada, compreendendo um óleo de xisto por hidroconversão em camada fervente, fracionamento por destilação atmosférica e extração líquido/líquido da fração pesada
IL226639A IL226639A (en) 2010-12-24 2013-05-29 A method for converting hydrocarbon raw materials containing oil shales through hydroconversion into a floating substrate, separating them into atmospheric distillation and extracting liquid / liquid from heavy components
MA36029A MA34751B1 (fr) 2010-12-24 2013-06-20 Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde.

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FR1061244A FR2969650B1 (fr) 2010-12-24 2010-12-24 Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde

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FR2969650B1 true FR2969650B1 (fr) 2014-04-11

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CN (1) CN103339233B (et)
AU (1) AU2011347041B2 (et)
BR (1) BR112013013951A2 (et)
CA (1) CA2815618C (et)
EE (1) EE05762B1 (et)
FR (1) FR2969650B1 (et)
IL (1) IL226639A (et)
MA (1) MA34751B1 (et)
RU (1) RU2592690C2 (et)
WO (1) WO2012085406A1 (et)

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US20140330057A1 (en) * 2013-05-02 2014-11-06 Shell Oil Company Process for converting a biomass material
FR3015514B1 (fr) 2013-12-23 2016-10-28 Total Marketing Services Procede ameliore de desaromatisation de coupes petrolieres
FR3030568B1 (fr) * 2014-12-18 2019-04-05 Axens Procede de conversion profonde de residus maximisant le rendement en gazole
FR3030567B1 (fr) * 2014-12-18 2017-02-03 Axens Procede de conversion profonde de residus maximisant le rendement en essence

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US2846358A (en) * 1956-03-06 1958-08-05 Exxon Research Engineering Co Removal of metal contaminants from heavy oils by hydrogenation followed by solvent extraction
US3306845A (en) * 1964-08-04 1967-02-28 Union Oil Co Multistage hydrofining process
US3472759A (en) * 1967-04-25 1969-10-14 Atlantic Richfield Co Process for removal of sulfur and metals from petroleum materials
US3954603A (en) * 1975-02-10 1976-05-04 Atlantic Richfield Company Method of removing contaminant from hydrocarbonaceous fluid
US4272362A (en) * 1980-02-01 1981-06-09 Suntech, Inc. Process to upgrade shale oil
US4483763A (en) 1982-12-27 1984-11-20 Gulf Research & Development Company Removal of nitrogen from a synthetic hydrocarbon oil
US4592827A (en) * 1983-01-28 1986-06-03 Intevep, S.A. Hydroconversion of heavy crudes with high metal and asphaltene content in the presence of soluble metallic compounds and water
US4764266A (en) * 1987-02-26 1988-08-16 Mobil Oil Corporation Integrated hydroprocessing scheme for production of premium quality distillates and lubricants
FR2617497B1 (fr) 1987-07-02 1989-12-08 Inst Francais Du Petrole Procede pour l'elimination de composes de l'arsenic dans les hydrocarbures liquides
US5059303A (en) * 1989-06-16 1991-10-22 Amoco Corporation Oil stabilization
US5164070A (en) * 1991-03-06 1992-11-17 Uop Hydrocracking product recovery process
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.
FR2683743B1 (fr) 1991-11-14 1994-02-11 Institut Francais Petrole Procede et dispositif d'echange thermique de particules solides pour double regeneration en craquage catalytique.
FR2705142B1 (fr) 1993-05-10 1995-10-27 Inst Francais Du Petrole Procede de regulation du niveau thermique d'un solide dans un echangeur de chaleur presentant des nappes cylindriques de tubes.
DE69708872T2 (de) * 1996-07-15 2002-04-11 Chevron U.S.A. Inc., San Ramon Schwefelbeständiger katalysator zur hydrokonversion und wasserstoffbehandlung von wasserstoffbehandlung von schwefelhältigen schmiermittelausgangsstoffen
FR2753984B1 (fr) * 1996-10-02 1999-05-28 Inst Francais Du Petrole Procede de conversion d'une fraction lourde d'hydrocarbures impliquant une hydrodemetallisation en lit bouillonnant de catalyseur
FR2762004B1 (fr) 1997-04-10 1999-05-14 Inst Francais Du Petrole Procede pour l'elimination d'arsenic dans les charges hydrocarbonees liquides
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CA2815618A1 (fr) 2012-06-28
AU2011347041B2 (en) 2015-11-19
AU2011347041A1 (en) 2013-05-16
US20130319911A1 (en) 2013-12-05
RU2592690C2 (ru) 2016-07-27
BR112013013951A2 (pt) 2016-09-27
IL226639A (en) 2017-06-29
EE201300023A (et) 2013-10-15
CN103339233A (zh) 2013-10-02
EE05762B1 (et) 2016-03-15
MA34751B1 (fr) 2013-12-03
WO2012085406A1 (fr) 2012-06-28
FR2969650A1 (fr) 2012-06-29
CA2815618C (fr) 2018-10-23
RU2013134382A (ru) 2015-01-27
CN103339233B (zh) 2015-07-29

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