NO20080060L - Fremgangsmate for a fremstille mellomdestillater ved hydroisomerisering og hydrocracking av ramaterialer utvunnet fra en Fischer-Tropsch prosess ved a anvende et multifunksjonelt sikkerhetssjikt - Google Patents

Fremgangsmate for a fremstille mellomdestillater ved hydroisomerisering og hydrocracking av ramaterialer utvunnet fra en Fischer-Tropsch prosess ved a anvende et multifunksjonelt sikkerhetssjikt

Info

Publication number
NO20080060L
NO20080060L NO20080060A NO20080060A NO20080060L NO 20080060 L NO20080060 L NO 20080060L NO 20080060 A NO20080060 A NO 20080060A NO 20080060 A NO20080060 A NO 20080060A NO 20080060 L NO20080060 L NO 20080060L
Authority
NO
Norway
Prior art keywords
fischer
hydroisomerization
hydrocracking
raw materials
preparing intermediate
Prior art date
Application number
NO20080060A
Other languages
English (en)
Other versions
NO341451B1 (no
Inventor
Patrick Euzen
Vincenzo Calemma
Original Assignee
Inst Francais Du Petrole
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 Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Publication of NO20080060L publication Critical patent/NO20080060L/no
Publication of NO341451B1 publication Critical patent/NO341451B1/no

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • 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
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/88Molybdenum
    • B01J23/883Molybdenum and nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/19Catalysts containing parts with different compositions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0207Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
    • CCHEMISTRY; METALLURGY
    • 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
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • CCHEMISTRY; METALLURGY
    • 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32Selective hydrogenation of the diolefin or acetylene compounds
    • C10G45/34Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
    • C10G45/36Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/38Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum or tungsten metals, or compounds thereof
    • CCHEMISTRY; METALLURGY
    • 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
    • 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
    • C10G47/14Inorganic carriers the catalyst containing platinum group metals or compounds thereof
    • CCHEMISTRY; METALLURGY
    • 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
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12Silica and alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/02Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/023Details
    • B01J2208/024Particulate material
    • B01J2208/025Two or more types of catalyst
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002Chemical plants
    • B01J2219/00027Process aspects
    • B01J2219/00038Processes in parallel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19Molybdenum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/615100-500 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63Pore volume
    • B01J35/6350.5-1.0 ml/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63Pore volume
    • B01J35/638Pore volume more than 1.0 ml/g
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S208/00Mineral oils: processes and products
    • Y10S208/95Processing of "fischer-tropsch" crude

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Oppfinnelsen angår en fremgangsmåte for fremstilling av mellomdestillater fra utløpsstrømmer oppnådd ved Fischer-Tropsch-syntese, omfattende et trinn for hydrogenbehandling og foredling og/eller dekontaminering ved å føre den over et multifunksjonelt forsjikt. Oppfinnelsen angår også et anlegg.
NO20080060A 2005-07-18 2008-01-04 Fremgangsmåte for fremstilling av mellomdestillater ved hydroisomerisering og hydrokrakking av råmaterialer utvunnet fra en Fischer-Tropsch-prosess ved anvendelse av et beskyttelsessjikt NO341451B1 (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0507576A FR2888584B1 (fr) 2005-07-18 2005-07-18 Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de charges issues du procede fischer-tropsch utilisant un lit de garde multifonctionnel
PCT/FR2006/001742 WO2007010126A2 (fr) 2005-07-18 2006-07-17 Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de charges issues du procede fischer-tropsch utilisant un lit de garde multifonctionnel

Publications (2)

Publication Number Publication Date
NO20080060L true NO20080060L (no) 2008-04-14
NO341451B1 NO341451B1 (no) 2017-11-13

Family

ID=36572353

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20080060A NO341451B1 (no) 2005-07-18 2008-01-04 Fremgangsmåte for fremstilling av mellomdestillater ved hydroisomerisering og hydrokrakking av råmaterialer utvunnet fra en Fischer-Tropsch-prosess ved anvendelse av et beskyttelsessjikt

Country Status (8)

Country Link
US (1) US7658836B2 (no)
EP (1) EP1907508B1 (no)
FR (1) FR2888584B1 (no)
NO (1) NO341451B1 (no)
PL (1) PL1907508T3 (no)
RU (1) RU2419650C2 (no)
WO (1) WO2007010126A2 (no)
ZA (1) ZA200800183B (no)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100885311B1 (ko) 2007-09-04 2009-02-24 한국화학연구원 피셔-트롭쉬 합성용 코발트/인-알루미나 촉매와 이의 제조방법
MY155825A (en) * 2007-09-10 2015-12-15 Shell Int Research A process for hydrocracking and hydro-isomerisation of a paraffinic feedstock
CN101835537B (zh) * 2007-09-17 2013-05-22 国际壳牌研究有限公司 用于使气体物流中含有的硫化合物催化还原的催化剂组合物及其制备方法和用途
BRPI0705939A2 (pt) * 2007-10-29 2009-06-23 Petroleo Brasileiro Sa processo para a produção de catalisadores hìbridos para a sìntese de fischer-tropsch e catalisador hìbrido produzido de acordo com o processo
FR2926085B1 (fr) * 2008-01-04 2010-02-12 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de charges issues du procede fischer-tropsch
US8038869B2 (en) * 2008-06-30 2011-10-18 Uop Llc Integrated process for upgrading a vapor feed
FR2944028B1 (fr) * 2009-04-03 2011-05-06 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage d'une fraction lourde issue d'un effluent fischer-tropsch mettant en oeuvre une resine
FR2944027B1 (fr) * 2009-04-03 2011-05-06 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage d'une fraction lourde issue d'un effluent fischer-tropsch
FR2970259B1 (fr) 2011-01-07 2014-07-18 IFP Energies Nouvelles Procede d'hydrocraquage utilisant un catalyseur zeolithique contenant deux fonctions hydrogenantes distinctes.
US20140005450A1 (en) * 2012-06-29 2014-01-02 Uop Llc Use of n-paraffin adsorption to increase selectivity and yield of synthetic distillate fuel
FR3018810B1 (fr) * 2014-03-20 2017-06-09 Ifp Energies Now Procede fischer-tropsch utilisant un catalyseur a base d'un metal du groupe viiib et d'un support d'oxydes comprenant de l'alumine, de la silice et du phosphore
FR3022157B1 (fr) * 2014-06-13 2017-09-01 Ifp Energies Now Catalyseur bimodal a phase active comalaxee, son procede de preparation et son utilisation en hydrotraitement de residus
CN104711019B (zh) * 2015-03-05 2016-09-14 武汉凯迪工程技术研究总院有限公司 利用费托合成油生产柴油和喷气燃料的系统及方法
US9956553B2 (en) * 2016-06-28 2018-05-01 Chevron U.S.A. Inc. Regeneration of an ionic liquid catalyst by hydrogenation using a macroporous noble metal catalyst
US10472581B2 (en) * 2016-06-30 2019-11-12 Uop Llc Process and apparatus for hydrocracking and hydroisomerizing a hydrocarbon stream
FR3084084B1 (fr) * 2018-07-18 2020-07-10 IFP Energies Nouvelles Procede de production d'olefines et de distillats moyens a partir d'un effluent hydrocarbone issu de la synhtese fischer-tropsch
RU2704123C1 (ru) * 2019-06-24 2019-10-24 Федеральное государственное бюджетное учреждение науки "Федеральный исследовательский центр "Институт катализа им. Г.К. Борескова Сибирского отделения Российской академии наук" (ИК СО РАН, Институт катализа СО РАН) Способ переработки тяжелого нефтяного сырья на защитном слое бифункционального катализатора
RU2704122C1 (ru) * 2019-06-24 2019-10-24 Федеральное государственное бюджетное учреждение науки "Федеральный исследовательский центр "Институт катализа им. Г.К. Борескова Сибирского отделения Российской академии наук" (ИК СО РАН, Институт катализа СО РАН) Способ переработки тяжелого нефтяного сырья на катализаторе защитного слоя
CN114630885B (zh) * 2019-12-24 2023-05-02 特殊设计和工程局卡塔利扎托尔股份公司 C3-c5链烷烃固定床脱氢催化剂及其生产用载体
RU2731568C1 (ru) * 2019-12-24 2020-09-04 Акционерное общество "Специальное конструкторско-технологическое бюро "Катализатор" Катализатор дегидрирования С3-С5 парафиновых углеводородов в стационарном слое

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4943672A (en) * 1987-12-18 1990-07-24 Exxon Research And Engineering Company Process for the hydroisomerization of Fischer-Tropsch wax to produce lubricating oil (OP-3403)
US4937218A (en) * 1988-09-06 1990-06-26 Intevep, S.A. Catalytic system for the hydroconversion of heavy oils
MY108862A (en) * 1992-08-18 1996-11-30 Shell Int Research Process for the preparation of hydrocarbon fuels
US5378348A (en) * 1993-07-22 1995-01-03 Exxon Research And Engineering Company Distillate fuel production from Fischer-Tropsch wax
AU2001249695A1 (en) * 2000-04-03 2001-10-15 Chevron U.S.A. Inc. Improved conversion of syngas to distillate fuels
FR2826971B1 (fr) * 2001-07-06 2003-09-26 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de charges issues du procede fischer-tropsch
FR2826972B1 (fr) * 2001-07-06 2007-03-23 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage d'une fraction lourde issue d'un effluent produit par le procede fischer-tropsch
FR2826973B1 (fr) * 2001-07-06 2005-09-09 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de 2 fractions issues de charges provenant du procede fischer-tropsch
FR2826974B1 (fr) * 2001-07-06 2007-03-23 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage en 2 etapes de charges issues du procede fischer-tropsch
FR2850393B1 (fr) * 2003-01-27 2005-03-04 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de charges issues du procede fischer-tropsch
US20040159582A1 (en) * 2003-02-18 2004-08-19 Simmons Christopher A. Process for producing premium fischer-tropsch diesel and lube base oils

Also Published As

Publication number Publication date
RU2008105913A (ru) 2009-08-27
PL1907508T3 (pl) 2014-09-30
ZA200800183B (en) 2009-04-29
FR2888584B1 (fr) 2010-12-10
WO2007010126A3 (fr) 2007-03-15
EP1907508B1 (fr) 2014-04-30
FR2888584A1 (fr) 2007-01-19
RU2419650C2 (ru) 2011-05-27
NO341451B1 (no) 2017-11-13
US7658836B2 (en) 2010-02-09
WO2007010126A2 (fr) 2007-01-25
EP1907508A2 (fr) 2008-04-09
US20070017850A1 (en) 2007-01-25

Similar Documents

Publication Publication Date Title
NO20080060L (no) Fremgangsmate for a fremstille mellomdestillater ved hydroisomerisering og hydrocracking av ramaterialer utvunnet fra en Fischer-Tropsch prosess ved a anvende et multifunksjonelt sikkerhetssjikt
NO20053434D0 (no) Fremgangsmate for fremstilling av mellomdestillater ved hydroisomeriserinq og hydrokrakking av fodestrommer fra Fischer Tropsch prosessen
NO20062678L (no) Fremgangsmate for a lage smoreoljegrunnrastoffer
EA200702548A1 (ru) Способ получения хлоргидрина из полигидроксилированного алифатического углеводорода
NO20081932L (no) Fremgangsmate for behandling av avlopsvann omfattende trinn for dekantering og finsortering, og anordning for a utfore nevnte fremgangsmate
FI20085400A0 (fi) Menetelmä jäteveden integroidulle käsittelylle
FR2892950B1 (fr) Traitement combine d'effluents gazeux par plasma froid et photocatatyse
ATE528300T1 (de) Bizyklische verbindungen und ihre verwendung als antidiabetika
MY146536A (en) Removal of carbon dioxide from a gas stream
NO20082909L (no) Fremgangsmate for a utvinne lignan-ekstrakter og sammensetninger inneholdende lignan-ekstraktene
NO20064660L (no) Nye forbindelser som opioid-reseptormodulatorer
ATE556105T1 (de) Substituierte organopolysiloxane und ihre verwendung
NO20072223L (no) Glykogenfosforylaseinhibitor forbindelser med farmsoytiske preparater av disse
NO20081983L (no) Nye azetidinforbindelser nyttige i behandlingen av funksjonelle gastrointestinale forstyrrelser, IBS og funksjonell dyspepsi
TW200745031A (en) Acyl indoles, compositions containing such compounds and methods of use
NO20081522L (no) Fremgangsmate for behandling av vann omfattende et raskt bunnfellingstrinn etterfulgt av et filtreringstrinn direkte pa mikro- eller ultrafiltreringsmenbraner, og tilhorende anordning
MX2010005648A (es) Derivados de alcano azabiciclico sustituidos con biarilo como moduladores de la actividad del receptor nicotinico de acetilcolina.
ATE543910T1 (de) Verfahren und materialien zur herstellung von simvastatin und verwandten verbindungen
NO20081562L (no) Syntetiske metoder og mellomprodukt for stereoisomeriske forbindelser som er nyttige for behandlingen av gastrointestinale og sentralnervesystemersykdommer
HK1145189A1 (en) Enzyme involved in synthesis of equol
MX2007004230A (es) Compuestos de tienopiridinona y metodos de tratamiento.
DE602006003393D1 (de) Verfahren zur Herstellung von Synthesegas durch Dampfreformieren und partielle Oxidation
NO20035836L (no) Fremgangsmate for fremstilling av mellomdestillater ved to-trinns hydroisomerisering og hydrokrakking av tilforsel fra Fischer-Tropsch prosessen
EA200800522A1 (ru) Способ депарафинизации при использовании цеолитов мтт и mtw
RU2011118231A (ru) Способ получения трихлорсилана и тетрахлорсилана

Legal Events

Date Code Title Description
MM1K Lapsed by not paying the annual fees