RU2013134377A - METHOD FOR CONVERSION OF HYDROCARBON RAW MATERIAL CONTAINING SHALE OIL, BY HYDROCONVERSION IN A BOILING LAYER, FRACTION USING ATMOSPHERIC DISTILLATION AND HYDROCRINE - Google Patents
METHOD FOR CONVERSION OF HYDROCARBON RAW MATERIAL CONTAINING SHALE OIL, BY HYDROCONVERSION IN A BOILING LAYER, FRACTION USING ATMOSPHERIC DISTILLATION AND HYDROCRINE Download PDFInfo
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- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
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- 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
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
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- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/002—Production 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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- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
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- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining 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
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- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining 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
- C10G45/04—Refining 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
- C10G45/06—Refining 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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- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining 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
- C10G45/04—Refining 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
- C10G45/06—Refining 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
- C10G45/08—Refining 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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- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking 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
- C10G47/12—Inorganic carriers
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- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
- C10G47/26—Cracking 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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- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
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- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/12—Treatment 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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- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/14—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only
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- 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
- C10G2300/1011—Biomass
- C10G2300/1014—Biomass of vegetal origin
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- 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
- C10G2300/1011—Biomass
- C10G2300/1018—Biomass of animal origin
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- 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
- C10G2300/1074—Vacuum distillates
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
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- 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
- C10G2300/4081—Recycling aspects
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- 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
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- 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
- C10G2400/04—Diesel oil
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- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/06—Gasoil
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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Abstract
1. Способ конверсии сланцевого масла или смеси сланцевых масел, имеющих содержание азота по меньшей мере 0,1%, часто по меньшей мере 1% и очень часто по меньшей мере 2 мас.%, отличающийся тем, что он содержит следующие стадии:a) сырье вводится в часть для гидроконверсии в присутствии водорода, причем указанная часть содержит по меньшей мере реактор с кипящем слоем, работающий в режиме газообразного и жидкого восходящего потока и содержащий по меньшей мере один катализатор гидроконверсии на подложке,b) выходящий поток, полученный на стадии a), вводится, по меньшей мере частично и часто полностью, в зону фракционирования, из которой, посредством атмосферной дистилляции, выходят газообразная фракция, фракция лигроина, фракция газойля и фракция, более тяжелая, чем фракция газойля,c) указанная фракция лигроина обрабатывается, по меньшей мере частично и часто полностью, в первой части для гидрообработки в присутствии водорода, причем указанная часть содержит по меньшей мере один реактор с фиксированным слоем, содержащий по меньшей мере один катализатор гидрообработки,d) указанная фракция газойля обрабатывается, по меньшей мере частично и часто полностью, во второй части для гидрообработки в присутствии водорода, причем указанная часть содержит по меньшей мере один реактор с фиксированным слоем, содержащий по меньшей мере один катализатор гидрообработки,e) фракция, более тяжелая, чем фракция газойля, обрабатывается, по меньшей мере частично и часто полностью, в части для гидрокрекинга в присутствии водорода.2. Способ по п.1, в котором выходящие потоки гидрокрекинга, полученные в конце стадии e), фракционируются на вторую газ�1. A process for converting shale oil or a mixture of shale oils having a nitrogen content of at least 0.1%, often at least 1% and very often at least 2% by weight, characterized in that it comprises the following steps: a) the feedstock is introduced into the hydroconversion part in the presence of hydrogen, said part comprising at least a fluidized bed reactor operating in gaseous and liquid upflow mode and containing at least one supported hydroconversion catalyst, b) the effluent stream obtained in step a ), is introduced, at least partially and often completely, into the fractionation zone, from which, by means of atmospheric distillation, a gaseous fraction, a naphtha fraction, a gas oil fraction and a fraction heavier than the gas oil fraction, c) said naphtha fraction is processed, according to at least partially and often completely, in the first part for hydroprocessing in the presence of hydrogen, and the specified part contains at least one reactor with fi d) said gas oil fraction is treated, at least partially and often completely, in a second part for hydroprocessing in the presence of hydrogen, said part containing at least one fixed bed reactor containing at least one hydrotreating catalyst, e) the fraction heavier than the gas oil fraction is treated at least partially and often completely in the hydrocracking part in the presence of hydrogen. Process according to claim 1, wherein the hydrocracking effluents obtained at the end of step e) are fractionated into a second gas�
Claims (19)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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FR1061246A FR2969648B1 (en) | 2010-12-24 | 2010-12-24 | HYDROCARBONATE CHARGING CONVERSION PROCESS COMPRISING SCHIST OIL BY BOILING BED HYDROCONVERSION, ATMOSPHERIC DISTILLATION FRACTIONATION, AND HYDROCRACKING |
FR1061246 | 2010-12-24 | ||
PCT/FR2011/053021 WO2012085407A1 (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 hydrocracking |
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RU2013134377A true RU2013134377A (en) | 2015-01-27 |
RU2592688C2 RU2592688C2 (en) | 2016-07-27 |
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RU2013134377/04A RU2592688C2 (en) | 2010-12-24 | 2011-12-16 | Method of converting hydrocarbon material containing shale oil by hydroconversion in fluidised bed, fractionation using atmospheric distillation and hydrocracking |
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US (1) | US20130319908A1 (en) |
CN (1) | CN103328613B (en) |
AU (1) | AU2011347042B2 (en) |
BR (1) | BR112013015358A2 (en) |
CA (1) | CA2816666C (en) |
EE (1) | EE05782B1 (en) |
FR (1) | FR2969648B1 (en) |
IL (1) | IL226641A (en) |
MA (1) | MA34752B1 (en) |
RU (1) | RU2592688C2 (en) |
WO (1) | WO2012085407A1 (en) |
Families Citing this family (14)
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US9080113B2 (en) | 2013-02-01 | 2015-07-14 | Lummus Technology Inc. | Upgrading raw shale-derived crude oils to hydrocarbon distillate fuels |
FR3004722B1 (en) * | 2013-04-23 | 2016-03-11 | IFP Energies Nouvelles | PROCESS FOR THE CONVERSION OF FUEL BASED RENEWABLE ORIGINAL LOADS COMPRISING A BOILING BED HYDROTREATMENT STEP AND A FIXED BED HYDROISOMERIZATION STEP |
CN104560173B (en) * | 2013-10-29 | 2016-11-16 | 中国石油化工股份有限公司 | A kind of heavy oil hydrogenation conversion method |
FR3015514B1 (en) | 2013-12-23 | 2016-10-28 | Total Marketing Services | IMPROVED PROCESS FOR DESAROMATIZATION OF PETROLEUM CUTTERS |
FR3030568B1 (en) * | 2014-12-18 | 2019-04-05 | Axens | PROCESS FOR DEEP CONVERSION OF RESIDUES MAXIMIZING GAS OUTPUT |
WO2016201254A1 (en) * | 2015-06-10 | 2016-12-15 | Saudi Arabian Oil Company | Characterizing crude oil using laser induced ultraviolet fluorescence spectroscopy |
US9803505B2 (en) | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated aromatics and naphtha block facilities |
US9803513B2 (en) * | 2015-08-24 | 2017-10-31 | Saudi Arabian Oil Company | Power generation from waste heat in integrated aromatics, crude distillation, and naphtha block facilities |
TWI736611B (en) * | 2016-04-25 | 2021-08-21 | 荷蘭商蜆殼國際研究所 | An ebullated bed process for high conversion of heavy hydrocarbons with a low sediment yield |
CN108079911B (en) * | 2016-11-21 | 2020-02-07 | 北京华石联合能源科技发展有限公司 | Reaction system for controlling cracking hydrogenation by upstream differential speed and application thereof |
US10457878B2 (en) * | 2017-09-20 | 2019-10-29 | Uop Llc | Process for recovering hydrocracked effluent |
AU2019368665A1 (en) * | 2018-10-24 | 2021-04-29 | Haldor Topsøe A/S | Method for production of aviation fuel |
FR3101082B1 (en) * | 2019-09-24 | 2021-10-08 | Ifp Energies Now | Integrated fixed bed hydrocracking and bubbling bed hydroconversion process with improved gas / liquid separation |
US11034895B1 (en) * | 2020-01-22 | 2021-06-15 | Axens SA | Process for production of on specification group III/III+ base oils while preserving base oil yield |
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US3954603A (en) * | 1975-02-10 | 1976-05-04 | Atlantic Richfield Company | Method of removing contaminant from hydrocarbonaceous fluid |
US4133745A (en) * | 1977-08-18 | 1979-01-09 | Atlantic Richfield Company | Processing shale oil cuts by hydrotreating and removal of arsenic and/or selenium |
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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 |
US4548702A (en) * | 1984-02-24 | 1985-10-22 | Standard Oil Company | Shale oil stabilization with a hydroprocessor |
US4764266A (en) * | 1987-02-26 | 1988-08-16 | Mobil Oil Corporation | Integrated hydroprocessing scheme for production of premium quality distillates and lubricants |
FR2617497B1 (en) | 1987-07-02 | 1989-12-08 | Inst Francais Du Petrole | PROCESS FOR THE REMOVAL OF ARSENIC COMPOUNDS FROM LIQUID HYDROCARBONS |
US5164070A (en) * | 1991-03-06 | 1992-11-17 | Uop | Hydrocracking product recovery process |
FR2753984B1 (en) * | 1996-10-02 | 1999-05-28 | Inst Francais Du Petrole | METHOD FOR CONVERTING A HEAVY HYDROCARBON FRACTION INVOLVING HYDRODEMETALLIZATION IN A BUBBLE BED OF CATALYST |
FR2762004B1 (en) | 1997-04-10 | 1999-05-14 | Inst Francais Du Petrole | PROCESS FOR THE REMOVAL OF ARSENIC FROM LIQUID HYDROCARBON FILLERS |
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ITMI20071198A1 (en) * | 2007-06-14 | 2008-12-15 | Eni Spa | IMPROVED PROCEDURE FOR THE HYDROCONVERSION OF HEAVY OILS WITH BULLETS |
FR2933708B1 (en) * | 2008-07-10 | 2011-07-22 | Inst Francais Du Petrole | CONVERSION PROCESS COMPRISING HYDROCONVERSION OF THE LOAD THEN A VISCOREDUCTION AND A FRACTIONATION |
US8151515B2 (en) * | 2009-07-27 | 2012-04-10 | Charles Eric Crouse | Device for the removal of arachnids, and method for removal of small arachnids and insects |
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2010
- 2010-12-24 FR FR1061246A patent/FR2969648B1/en not_active Expired - Fee Related
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2011
- 2011-12-16 WO PCT/FR2011/053021 patent/WO2012085407A1/en active Application Filing
- 2011-12-16 US US13/997,330 patent/US20130319908A1/en not_active Abandoned
- 2011-12-16 CN CN201180062159.0A patent/CN103328613B/en not_active Expired - Fee Related
- 2011-12-16 CA CA2816666A patent/CA2816666C/en not_active Expired - Fee Related
- 2011-12-16 AU AU2011347042A patent/AU2011347042B2/en not_active Ceased
- 2011-12-16 BR BR112013015358A patent/BR112013015358A2/en not_active IP Right Cessation
- 2011-12-16 RU RU2013134377/04A patent/RU2592688C2/en not_active IP Right Cessation
- 2011-12-16 EE EEP201300024A patent/EE05782B1/en not_active IP Right Cessation
-
2013
- 2013-05-29 IL IL226641A patent/IL226641A/en not_active IP Right Cessation
- 2013-06-20 MA MA36030A patent/MA34752B1/en unknown
Also Published As
Publication number | Publication date |
---|---|
FR2969648B1 (en) | 2014-04-11 |
RU2592688C2 (en) | 2016-07-27 |
FR2969648A1 (en) | 2012-06-29 |
CN103328613B (en) | 2016-03-23 |
CA2816666C (en) | 2018-10-23 |
MA34752B1 (en) | 2013-12-03 |
CA2816666A1 (en) | 2012-06-28 |
AU2011347042B2 (en) | 2015-11-19 |
EE201300024A (en) | 2013-10-15 |
AU2011347042A1 (en) | 2013-05-09 |
WO2012085407A8 (en) | 2013-07-11 |
IL226641A (en) | 2017-05-29 |
BR112013015358A2 (en) | 2017-07-18 |
WO2012085407A1 (en) | 2012-06-28 |
CN103328613A (en) | 2013-09-25 |
EE05782B1 (en) | 2016-11-15 |
US20130319908A1 (en) | 2013-12-05 |
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