ES2138731T3 - Procedimiento de tratamiento con hidroisomerizacion de cargas procedentes del procedimiento fischer-tropsch. - Google Patents

Procedimiento de tratamiento con hidroisomerizacion de cargas procedentes del procedimiento fischer-tropsch.

Info

Publication number
ES2138731T3
ES2138731T3 ES95914400T ES95914400T ES2138731T3 ES 2138731 T3 ES2138731 T3 ES 2138731T3 ES 95914400 T ES95914400 T ES 95914400T ES 95914400 T ES95914400 T ES 95914400T ES 2138731 T3 ES2138731 T3 ES 2138731T3
Authority
ES
Spain
Prior art keywords
procedure
hydroisomerization
noble metal
loads
fischer
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
ES95914400T
Other languages
English (en)
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
Application granted granted Critical
Publication of ES2138731T3 publication Critical patent/ES2138731T3/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
    • C10G45/58—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)

Abstract

LA INVENCION SE REFIERE A UN PROCEDIMIENTO DE TRATAMIENTO CON HIDROISOMERIZACION DE CARGAS OBTENIDAS DEL PROCEDIMIENTO FISCHERTROPSCH. EL CATALIZADOR ESTA ESENCIALMENTE CONSTITUIDO POR 0,05% A 10% EN PESO DE METAL NOBLE POR UN SOPORTE DE SILICE (570%)/ALUMINA QUE TIENE UNA SUPERFICIE ESPECIFICA DE 100-500 M{SUP,2}/G. EL CATALIZADOR PRESENTA UN DIAMETRO MEDIO DE POROS DE 1-12 NM, EL VOLUMEN POROSO DE LOS POROS CUYO DIAMETRO ESTA COMPRENDIDO ENTRE EL DIAMETRO MEDIO +/- 3NM ES SUPERIOR A 40% DEL VOLUMEN POROSO TOTAL, LA DISPERSION DE METAL NOBLE ES DE 20100% Y EL COEFICIENTE DE DISTRIBUCION DEL METAL NOBLE SUPERIOR A 0,1. EL PROCEDIMIENTO OPERA ENTRE 200-450 (GRADOS) C BAJO UNA PRESION PARCIAL DE HIDROGENO DE 2 A 25MPA CON UNA VVH DE 0,01-10 H{SUP,11} Y UNA TASA VOLUMINICA HIDROGENO/HIDROCARBURO DE 100-2000.
ES95914400T 1994-04-01 1995-03-22 Procedimiento de tratamiento con hidroisomerizacion de cargas procedentes del procedimiento fischer-tropsch. Expired - Lifetime ES2138731T3 (es)

Applications Claiming Priority (1)

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.

Publications (1)

Publication Number Publication Date
ES2138731T3 true ES2138731T3 (es) 2000-01-16

Family

ID=9461667

Family Applications (1)

Application Number Title Priority Date Filing Date
ES95914400T Expired - Lifetime ES2138731T3 (es) 1994-04-01 1995-03-22 Procedimiento de tratamiento con hidroisomerizacion de cargas procedentes del procedimiento fischer-tropsch.

Country Status (11)

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

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DZ2129A1 (fr) * 1995-11-28 2002-07-23 Shell Int Research Procédé pour produire des huiles lubrifiantes de base.
US6059955A (en) * 1998-02-13 2000-05-09 Exxon Research And Engineering Co. Low viscosity lube basestock
US6383366B1 (en) * 1998-02-13 2002-05-07 Exxon Research And Engineering Company Wax hydroisomerization process
EP1062306B1 (en) * 1998-02-13 2017-08-09 ExxonMobil Research and Engineering Company A lube basestock with excellent low temperature properties and a method for making
US20040112792A1 (en) * 1998-02-13 2004-06-17 Murphy William J. Method for making lube basestocks
EP1054942A4 (en) * 1998-02-13 2006-07-26 Exxonmobil Res & Eng Co PREPARATION OF LUBRICATING OILS WITH A CATALYST CONTAINER SYSTEM
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
EP1454669A1 (en) 1998-12-25 2004-09-08 Tosoh Corporation Combustion catalysts and processes for removing organic compounds
ES2185445B1 (es) * 1999-04-29 2004-08-16 Institut Francais Du Petrole Procedimiento flexible de produccion de bases de aceites y destilados medios con una conversion-hidroisomerizacion seguida de un desparafinado catalitico.
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
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
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
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
NL1015035C2 (nl) * 1999-04-29 2001-02-12 Inst Francais Du Petrole Flexibel proces voor de productie van basisoliÙn en destillatieproducten door een omzetting-hydroisomerisatie op een weinig gedispergeerde katalysator, gevolgd door een katalytische ontparaffinering.
JP4860861B2 (ja) * 1999-07-26 2012-01-25 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 潤滑基油を製造する方法
AU7725200A (en) * 1999-09-30 2001-04-30 Virginia Tech Intellectual Properties, Inc. Novel transition metal phosphide catalysts
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
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
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
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
CN111056949B (zh) * 2018-10-17 2021-05-11 中国石油化工股份有限公司 连续反应、再生、活化制苯胺反应装置及反应方法

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FR2563120A1 (fr) * 1984-04-23 1985-10-25 Leuna Werke Veb Catalyseur pour le reformage d'hydrocarbures, et procede pour sa fabrication
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Also Published As

Publication number Publication date
KR960702859A (ko) 1996-05-23
EP0725810A1 (fr) 1996-08-14
ZA952674B (en) 1996-09-30
FR2718145B1 (fr) 1996-05-31
FR2718145A1 (fr) 1995-10-06
CN1044130C (zh) 1999-07-14
KR100336725B1 (ko) 2002-12-05
NO954877L (no) 1995-11-30
JP3658671B2 (ja) 2005-06-08
EP0725810B1 (fr) 1999-09-08
CN1125960A (zh) 1996-07-03
NO954877D0 (no) 1995-11-30
DE69512017D1 (de) 1999-10-14
JPH08511302A (ja) 1996-11-26
DE69512017T2 (de) 2000-03-02
US5834522A (en) 1998-11-10
NO315123B1 (no) 2003-07-14
WO1995027020A1 (fr) 1995-10-12

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