ES2105762T3 - Procedimiento de hidrocraqueo e hidrodesparafinado. - Google Patents

Procedimiento de hidrocraqueo e hidrodesparafinado.

Info

Publication number
ES2105762T3
ES2105762T3 ES94928879T ES94928879T ES2105762T3 ES 2105762 T3 ES2105762 T3 ES 2105762T3 ES 94928879 T ES94928879 T ES 94928879T ES 94928879 T ES94928879 T ES 94928879T ES 2105762 T3 ES2105762 T3 ES 2105762T3
Authority
ES
Spain
Prior art keywords
hydrofracturing
zone
hydrogen
catalyst
contact
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 - Lifetime
Application number
ES94928879T
Other languages
English (en)
Inventor
Johannes Wilhelmus M Sonnemans
Franciscus Maria Nooij
Jacques Francois Jea Grootjans
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.)
TotalEnergies Onetech Belgium SA
Akzo Nobel NV
Original Assignee
Fina Research SA
Akzo Nobel NV
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=26134029&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ES2105762(T3) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Fina Research SA, Akzo Nobel NV filed Critical Fina Research SA
Application granted granted Critical
Publication of ES2105762T3 publication Critical patent/ES2105762T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • 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
    • C10G45/12—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 crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • C10G45/64—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00—Engines characterised by air compression and subsequent fuel addition
    • F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Steroid Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Superconductors And Manufacturing Methods Therefor (AREA)

Abstract

SE PRESENTA UN PROCESO PARA REDUCIR EL CONTENIDO DE CERA DE SUMINISTROS DE HIDROCARBONO QUE CONTENGAN CERA PARA PRODUCIR PRODUCTOS SEMIDESTILADOS QUE INCLUYEN COMBUSTIBLES DE INYECCION DE BAJO PUNTO DE CONGELACION Y/O COMBUSTIBLES DIESEL Y ACEITES DE CALEFACCION DE BAJO PUNTO DE FUSION Y DE BAJO PUNTO DE EVAPORACION. EL PROCESO COMPRENDE LA PUESTA EN CONTACTO DEL SUMINISTRO HIDROCARBONACEO CON UN CATALIZADOR HIDROFRACTURADOR QUE CONTIENE UN PORTADOR, AL MENOS UN COMPONENTE DE METAL DE HIDROGENACION SELECCIONADO ENTRE METALES DEL GRUPO VI Y DEL GRUPO VIII, Y UN ZEOLITO DE PORO GRANDE, POR EJEMPLO UN ZEOLITO DE TIPO Y, EN UNA ZONA DE HIDROFRACTURACION EN LA PRESENCIA DE HIDROGENO A UNA ELEVADA TEMPERATURA Y PRESION, Y LA PUESTA EN CONTACTO DEL EFLUYENTE COMPLETO DE LA ZONA DE HIDROFRACTURACION CON UN CATALIZADOR DE DESCERACION QUE CONTIENE UN TAMIZ MOLECULAR DE TAMAÑO DE PORO INTERMEDIO, CRISTALINO SELECCIONADO ENTRE METALOSILICATOS, POR EJEMPLO BOROSILICATOS, FERROSILICATOS Y ALUMINOSILICATOS, Y SILICOALUMINOFOSFATOS, POR EJEMPLO, SAPO-11, EN UNA ZONA DE DESHIDRODESCERACION EN LA PRESENCIA DE HIDROGENO A TEMPERATURA Y PRESION ELEVADAS.
ES94928879T 1993-10-08 1994-10-07 Procedimiento de hidrocraqueo e hidrodesparafinado. Expired - Lifetime ES2105762T3 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP93202853 1993-10-08
SG1996003552A SG48893A1 (en) 1993-10-08 1994-10-07 Hydrocracking and hydrodewaxing process

Publications (1)

Publication Number Publication Date
ES2105762T3 true ES2105762T3 (es) 1997-10-16

Family

ID=26134029

Family Applications (1)

Application Number Title Priority Date Filing Date
ES94928879T Expired - Lifetime ES2105762T3 (es) 1993-10-08 1994-10-07 Procedimiento de hidrocraqueo e hidrodesparafinado.

Country Status (19)

Country Link
US (1) US5935414A (es)
EP (1) EP0722478B1 (es)
JP (1) JP3665069B2 (es)
KR (1) KR100199849B1 (es)
CN (1) CN1046755C (es)
AT (1) ATE155519T1 (es)
AU (1) AU683938B2 (es)
BR (1) BR9407765A (es)
CA (1) CA2173599C (es)
CZ (1) CZ293108B6 (es)
DE (1) DE69404320T2 (es)
ES (1) ES2105762T3 (es)
FI (1) FI961532L (es)
HU (1) HU217791B (es)
NO (1) NO961379D0 (es)
PL (1) PL178305B1 (es)
RU (1) RU2128681C1 (es)
SG (1) SG48893A1 (es)
WO (1) WO1995010578A1 (es)

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FR2797270B1 (fr) * 1999-08-02 2003-03-07 Inst Francais Du Petrole Procede et flexible de production de bases huiles et eventuellement de distillats moyens de tres haute qualite
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FR2785617B1 (fr) * 1998-11-06 2001-01-05 Inst Francais Du Petrole Procede flexible de production de bases huiles et eventuellement de distillats moyens de tres haute qualite
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JP4769110B2 (ja) * 2006-03-30 2011-09-07 Ｊｘ日鉱日石エネルギー株式会社 ワックスの水素化分解方法
JP2007270061A (ja) * 2006-03-31 2007-10-18 Nippon Oil Corp 液体燃料基材の製造方法
RU2437716C2 (ru) * 2006-11-21 2011-12-27 Ниппон Ойл Корпорейшн Способ производства жидкого топлива
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RU2359995C1 (ru) * 2008-01-09 2009-06-27 Институт химии нефти Сибирского отделения Российской академии наук Способ депарафинизации тяжелых фракций высокопарафинистых нефтей
RU2362797C1 (ru) * 2008-05-22 2009-07-27 Общество с ограниченной ответственностью "Объединенный центр исследований и разработок" Способ получения деароматизированного дизельного топлива с ультранизким содержанием серы
US8431014B2 (en) * 2009-10-06 2013-04-30 Chevron U.S.A. Inc. Process and catalyst system for improving dewaxing catalyst stability and lubricant oil yield
CN102145291B (zh) * 2010-02-10 2013-09-25 中国石油化工股份有限公司 一种加氢裂化催化剂及其制备方法及烃油裂化方法
KR101354235B1 (ko) * 2010-04-14 2014-02-13 에스케이이노베이션 주식회사 수소화 탈왁스 공정을 위한 촉매 및 이의 제조 방법
CN102485332B (zh) * 2010-12-03 2013-10-16 中国石油天然气股份有限公司 一种含分子筛的馏分油加氢脱酸催化剂及其制备和应用
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Also Published As

Publication number Publication date
PL178305B1 (pl) 2000-04-28
AU683938B2 (en) 1997-11-27
CA2173599A1 (en) 1995-04-20
EP0722478A1 (en) 1996-07-24
WO1995010578A1 (en) 1995-04-20
PL313868A1 (en) 1996-07-22
AU7812594A (en) 1995-05-04
SG48893A1 (en) 1998-05-18
DE69404320D1 (de) 1997-08-21
CN1046755C (zh) 1999-11-24
KR100199849B1 (ko) 1999-06-15
JP3665069B2 (ja) 2005-06-29
CZ99196A3 (en) 1996-09-11
FI961532A0 (fi) 1996-04-04
BR9407765A (pt) 1997-03-18
ATE155519T1 (de) 1997-08-15
RU2128681C1 (ru) 1999-04-10
NO961379L (no) 1996-04-03
US5935414A (en) 1999-08-10
CZ293108B6 (cs) 2004-02-18
CN1132522A (zh) 1996-10-02
FI961532A7 (fi) 1996-04-04
CA2173599C (en) 2004-07-20
HU9600895D0 (en) 1996-06-28
FI961532L (fi) 1996-04-04
JPH09503541A (ja) 1997-04-08
HU217791B (hu) 2000-04-28
DE69404320T2 (de) 1998-01-29
HUT75022A (en) 1997-03-28
EP0722478B1 (en) 1997-07-16
NO961379D0 (no) 1996-04-03

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