DE69512017T2 - Verfahren zur behandlung duch hydroisomerizierung von einsätze aus fisher-tropshverfahren - Google Patents

Verfahren zur behandlung duch hydroisomerizierung von einsätze aus fisher-tropshverfahren

Info

Publication number
DE69512017T2
DE69512017T2 DE69512017T DE69512017T DE69512017T2 DE 69512017 T2 DE69512017 T2 DE 69512017T2 DE 69512017 T DE69512017 T DE 69512017T DE 69512017 T DE69512017 T DE 69512017T DE 69512017 T2 DE69512017 T2 DE 69512017T2
Authority
DE
Germany
Prior art keywords
tropsh
hydroisomerizing
fisher
inserts
treating
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
DE69512017T
Other languages
English (en)
Other versions
DE69512017D1 (de
Inventor
Samuel Mignard
Nathalie Marchal
Slavik Kasztelan
Pierre-Henri Bigeard
Alain Billon
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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 IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of DE69512017D1 publication Critical patent/DE69512017D1/de
Application granted granted Critical
Publication of DE69512017T2 publication Critical patent/DE69512017T2/de
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
    • C10G45/58—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
    • C10G45/62—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 platinum group metals or compounds thereof
    • 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12—Silica and alumina
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/615—100-500 m2/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63—Pore volume
    • B01J35/635—0.5-1.0 ml/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/643—Pore diameter less than 2 nm
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66—Pore distribution

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
DE69512017T 1994-04-01 1995-03-22 Verfahren zur behandlung duch hydroisomerizierung von einsätze aus fisher-tropshverfahren Expired - Lifetime DE69512017T2 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9403869A FR2718145B1 (fr) 1994-04-01 1994-04-01 Procédé de traitement avec hydroisomérisation de charges issues du procédé fischer-tropsch.
PCT/FR1995/000353 WO1995027020A1 (fr) 1994-04-01 1995-03-22 Procede de traitement avec hydroisomerisation de charges issues du procede fischer-tropsch

Publications (2)

Publication Number Publication Date
DE69512017D1 DE69512017D1 (de) 1999-10-14
DE69512017T2 true DE69512017T2 (de) 2000-03-02

Family

ID=9461667

Family Applications (1)

Application Number Title Priority Date Filing Date
DE69512017T Expired - Lifetime DE69512017T2 (de) 1994-04-01 1995-03-22 Verfahren zur behandlung duch hydroisomerizierung von einsätze aus fisher-tropshverfahren

Country Status (11)

Country Link
US (1) US5834522A (de)
EP (1) EP0725810B1 (de)
JP (1) JP3658671B2 (de)
KR (1) KR100336725B1 (de)
CN (1) CN1044130C (de)
DE (1) DE69512017T2 (de)
ES (1) ES2138731T3 (de)
FR (1) FR2718145B1 (de)
NO (1) NO315123B1 (de)
WO (1) WO1995027020A1 (de)
ZA (1) ZA952674B (de)

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DZ2129A1 (fr) * 1995-11-28 2002-07-23 Shell Int Research Procédé pour produire des huiles lubrifiantes de base.
US20040112792A1 (en) * 1998-02-13 2004-06-17 Murphy William J. Method for making lube basestocks
EP1054942A4 (de) * 1998-02-13 2006-07-26 Exxonmobil Res & Eng Co Herstellung von schmierölen mit einem katalysatorverbundsystem
JP2002503755A (ja) 1998-02-13 2002-02-05 エクソンモービル リサーチ アンド エンジニアリング カンパニー 低温特性に優れた潤滑用基材油及びその製造方法
US6383366B1 (en) * 1998-02-13 2002-05-07 Exxon Research And Engineering Company Wax hydroisomerization process
US6059955A (en) * 1998-02-13 2000-05-09 Exxon Research And Engineering Co. Low viscosity lube basestock
CN1096296C (zh) * 1998-11-13 2002-12-18 中国石油化工集团公司 一种生产中间馏分油的加氢裂化催化剂及其制备
EP1013332B1 (de) * 1998-12-25 2005-06-08 Tosoh Corporation Verbrennungskatalysatoren und Verfahren zur Entfernung von organischen Verbindungen
ES2190303B1 (es) * 1999-04-29 2005-02-16 Institut Francais Du Petrole Procedimiento flexible de produccion de bases de aceites y destilados para una conversion-hidroisomerizacion sobre un catalizador ligeramente disperso seguida de un desparafinado catalitico.
FR2792945B1 (fr) * 1999-04-29 2006-01-13 Inst Francais Du Petrole Procede de production de bases huiles et distillats moyens avec une conversion-hydroisomerisation suivie d'un deparaffinage catalytique
FR2805543B1 (fr) * 2000-02-24 2003-09-05 Inst Francais Du Petrole Procede flexible de production de bases huiles et distillats moyens avec une conversion-hydroisomerisation suivie d'un deparaffinage catalytique
FR2792946B1 (fr) * 1999-04-29 2003-10-24 Inst Francais Du Petrole Procede de production de bases huiles et de distillats moyens a partir de charges hydrocarbonees par une conversion-hydroisomerisation sur un catalyseur faiblement disperse suivie d'un deparaffinage catalytique
FR2805542B1 (fr) * 2000-02-24 2003-09-05 Inst Francais Du Petrole Procede flexible de production de bases huiles et de distillats par une conversion-hydroisomerisation sur un catalyseur faiblement disperse suivie d'un deparaffinage catalytique
FR2792851B1 (fr) * 1999-04-29 2002-04-05 Inst Francais Du Petrole Catalyseur a base de metal noble faiblement disperse et son utilisation pour la conversion de charges hydrocarbonees
NL1015036C2 (nl) * 1999-04-29 2001-02-12 Inst Francais Du Petrole Flexibel proces voor de productie van basisoliÙn en gemiddelde destillatieproducten met een omzetting-hydro-isomerisatie gevolgd door een katalytische ontparaffinering.
EP1240276A4 (de) * 1999-09-30 2003-07-02 Shigeo T Oyama Neuartiger übergangsmetallphosphid katalysator
KR100353412B1 (ko) * 2000-01-31 2002-09-18 한국과학기술원 탈왁스 공정용 금속함유 이원촉매의 제조방법
FR2812301B1 (fr) 2000-07-26 2003-04-04 Inst Francais Du Petrole Procede flexible de production de bases huiles et de distillats moyens a partir de charge contenant des heteroatomes
TW507587U (en) * 2001-07-13 2002-10-21 Jin-Shiang Chen Exercise device
US7077947B2 (en) * 2002-10-08 2006-07-18 Exxonmobil Research And Engineering Company Process for preparing basestocks having high VI using oxygenated dewaxing catalyst
US6995112B2 (en) 2002-11-08 2006-02-07 Chevron U.S.A. Inc. Highly homogeneous amorphous silica-alumina catalyst composition
FR2851569B1 (fr) * 2003-02-21 2007-04-20 Inst Francais Du Petrole Procede d'hydrocraquage en deux etapes utilisant un catalyseur amorphe a base de platine et de palladium
WO2005005644A1 (en) 2003-07-11 2005-01-20 Cytos Biotechnology Ag Gene expression system
US7348293B2 (en) * 2003-12-05 2008-03-25 Chevron U.S.A. Inc. Homogeneous modified-alumina Fischer-Tropsch catalyst supports
US20080032886A1 (en) * 2006-08-03 2008-02-07 Abb Lummus Global, Inc. Doped solid acid catalyst composition, process of conversion using same and conversion products thereof
EA019078B1 (ru) 2009-01-30 2013-12-30 Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн Способ повышения качества синтетической нефти, синтезированной по реакции синтеза фишера-тропша, и смешанной сырой нефти
US8268897B2 (en) 2010-05-28 2012-09-18 The University Of Kentucky Research Foundation Incorporation of catalytic dehydrogenation into Fischer-Tropsch synthesis to lower carbon dioxide emissions
US8309616B2 (en) 2010-05-28 2012-11-13 University Of Kentucky Research Foundation Incorporation of catalytic dehydrogenation into fischer-tropsch synthesis to significantly reduce carbon dioxide emissions
JP5693332B2 (ja) * 2011-03-31 2015-04-01 独立行政法人石油天然ガス・金属鉱物資源機構 再生水素化精製触媒及び炭化水素油の製造方法
FR2991198B1 (fr) * 2012-05-30 2015-05-15 IFP Energies Nouvelles Procede de preparation d'un catalyseur mettant en oeuvre au moins une etape de sechage rapide et au moins une etape de sechage en lit fluidise et son utilisation pour la synthese fischer-tropsch
CN110964564A (zh) * 2018-09-29 2020-04-07 内蒙古伊泰煤基新材料研究院有限公司 一种费托合成基钻井液基础油及其制备方法

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JPS5141641B2 (de) * 1972-01-06 1976-11-11
US4419271A (en) * 1979-10-15 1983-12-06 Union Oil Company Of California Hydrocarbon conversion catalyst
FR2563120A1 (fr) * 1984-04-23 1985-10-25 Leuna Werke Veb Catalyseur pour le reformage d'hydrocarbures, et procede pour sa fabrication
DE3880455T2 (de) * 1987-12-18 1993-09-16 Exxon Research Engineering Co Verfahren zur isomerisierung von wachs zu schmierbasisoelen.
DE3870429D1 (de) * 1987-12-18 1992-05-27 Exxon Research Engineering Co Verfahren zur hydroisomerisierung von fischer-tropsch-wachs zur herstellung von schmieroel.
US5151172A (en) * 1991-05-03 1992-09-29 Amoco Corporation Distillate hydrogenation
GB9119495D0 (en) * 1991-09-12 1991-10-23 Shell Int Research Process for the preparation of hydrocarbon fuels
US5187138A (en) * 1991-09-16 1993-02-16 Exxon Research And Engineering Company Silica modified hydroisomerization catalyst
US5248409A (en) * 1992-02-27 1993-09-28 Exxon Research & Engineering Company Metal on rare earth modified silica alumina as hydrocarbon conversion catalyst

Also Published As

Publication number Publication date
CN1044130C (zh) 1999-07-14
NO954877D0 (no) 1995-11-30
DE69512017D1 (de) 1999-10-14
US5834522A (en) 1998-11-10
FR2718145B1 (fr) 1996-05-31
FR2718145A1 (fr) 1995-10-06
NO954877L (no) 1995-11-30
KR960702859A (ko) 1996-05-23
ZA952674B (en) 1996-09-30
ES2138731T3 (es) 2000-01-16
JPH08511302A (ja) 1996-11-26
EP0725810A1 (de) 1996-08-14
EP0725810B1 (de) 1999-09-08
JP3658671B2 (ja) 2005-06-08
NO315123B1 (no) 2003-07-14
WO1995027020A1 (fr) 1995-10-12
KR100336725B1 (ko) 2002-12-05
CN1125960A (zh) 1996-07-03

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Legal Events

Date Code Title Description
8364 No opposition during term of opposition
8328 Change in the person/name/address of the agent

Representative=s name: VONNEMANN, KLOIBER & KOLLEGEN, 80796 MUENCHEN

8327 Change in the person/name/address of the patent owner

Owner name: IFP ENERGIES NOUVELLES, RUEIL-MALMAISON, FR

8328 Change in the person/name/address of the agent

Representative=s name: VONNEMANN, KLOIBER & KOLLEGEN, 81667 MUENCHEN