NO20001190L - Katalytisk blanding og fremgangsmÕte for fremstilling derav - Google Patents

Katalytisk blanding og fremgangsmÕte for fremstilling derav

Info

Publication number
NO20001190L
NO20001190L NO20001190A NO20001190A NO20001190L NO 20001190 L NO20001190 L NO 20001190L NO 20001190 A NO20001190 A NO 20001190A NO 20001190 A NO20001190 A NO 20001190A NO 20001190 L NO20001190 L NO 20001190L
Authority
NO
Norway
Prior art keywords
metal
preparation
hydrocarbon mixtures
catalytic
catalytic system
Prior art date
Application number
NO20001190A
Other languages
English (en)
Norwegian (no)
Other versions
NO20001190D0 (no
Inventor
Laura Maria Zanibelli
Marco Ferrari
Virginio Arrigoni
Original Assignee
Agip Petroli
Enitecnologie Spa
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 Agip Petroli, Enitecnologie Spa filed Critical Agip Petroli
Publication of NO20001190D0 publication Critical patent/NO20001190D0/no
Publication of NO20001190L publication Critical patent/NO20001190L/no

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
    • 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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
    • B01J29/78—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J29/7815—Zeolite Beta
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/03—Precipitation; Co-precipitation
    • B01J37/031—Precipitation
    • B01J37/033—Using Hydrolysis
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/03—Precipitation; Co-precipitation
    • B01J37/036—Precipitation; Co-precipitation to form a gel or a cogel
    • 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
    • C10G45/06—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
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
    • C10G49/08—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10—After treatment, characterised by the effect to be obtained
    • B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10—After treatment, characterised by the effect to be obtained
    • B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/34—Reaction with organic or organometallic compounds
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Dispersion Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
NO20001190A 1999-03-12 2000-03-08 Katalytisk blanding og fremgangsmÕte for fremstilling derav NO20001190L (no)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT1999MI000504A IT1311512B1 (it) 1999-03-12 1999-03-12 Composizione catalitica per l'upgrading di miscele idrocarburiche.

Publications (2)

Publication Number Publication Date
NO20001190D0 NO20001190D0 (no) 2000-03-08
NO20001190L true NO20001190L (no) 2000-09-13

Family

ID=11382256

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20001190A NO20001190L (no) 1999-03-12 2000-03-08 Katalytisk blanding og fremgangsmÕte for fremstilling derav

Country Status (15)

Country Link
US (3) US6803337B1 (fr)
EP (2) EP1637224A3 (fr)
JP (1) JP2000279816A (fr)
CN (1) CN100374530C (fr)
AT (1) ATE317296T1 (fr)
AU (1) AU778458B2 (fr)
BR (1) BR0001279A (fr)
CA (1) CA2300230C (fr)
DE (1) DE60025880T2 (fr)
DK (1) DK1034841T3 (fr)
ES (1) ES2257263T3 (fr)
IT (1) IT1311512B1 (fr)
NO (1) NO20001190L (fr)
PT (1) PT1034841E (fr)
RU (1) RU2245191C2 (fr)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1311512B1 (it) * 1999-03-12 2002-03-13 Agip Petroli Composizione catalitica per l'upgrading di miscele idrocarburiche.
JP4545328B2 (ja) * 2001-02-15 2010-09-15 コスモ石油株式会社 炭化水素油用水素化処理触媒の製造方法及び炭化水素油の水素化処理方法
EP1403358A1 (fr) * 2002-09-27 2004-03-31 ENI S.p.A. Procédé et catalysateurs pour la désulfuration profonde de carburants
US20050023191A1 (en) * 2003-08-01 2005-02-03 Shih Stuart S. Process to manufacture low sulfur fuels
US7012167B2 (en) * 2003-10-08 2006-03-14 Lyondell Chemical Technology, L.P. Diisobutylene process
US7745372B2 (en) 2003-12-22 2010-06-29 China Petroleum & Chemical Corporation Catalyst for selective hydrogenation of olefins and its preparation as well as use
CN100513530C (zh) * 2004-10-29 2009-07-15 中国石油化工股份有限公司 一种溶剂油的加氢改质方法
CN100497541C (zh) * 2004-10-29 2009-06-10 中国石油化工股份有限公司 一种重馏分油加氢处理催化剂及其制备方法
US20060111598A1 (en) * 2004-11-22 2006-05-25 Shaw-Chan Lin Diisobutylene process
MXPA05009283A (es) 2005-08-31 2007-02-27 Mexicano Inst Petrol Procedimiento para la preparacion de una composicion catalitica para el hidroprocesamiento de fracciones del petroleo.
CN101314133B (zh) * 2007-06-01 2012-05-30 亚申科技研发中心（上海）有限公司 反式-2-己烯酸催化加氢制备己酸的工艺
CN101357338B (zh) * 2007-07-30 2011-11-30 南京大学 一种用于FCC石脑油中烯烃骨架异构的Co/Co-MCM-41催化剂
RU2353644C1 (ru) * 2007-11-14 2009-04-27 Открытое акционерное общество "Ангарская нефтехимическая компания" (ОАО АНХК) Способ гидроочистки нефтяных фракций
JP5228064B2 (ja) * 2008-01-28 2013-07-03 エクソンモービル・ケミカル・パテンツ・インク メタンからの芳香族化合物の製造
ITMI20081061A1 (it) 2008-06-11 2009-12-12 Eni Spa Sistema catalitico e procedimento per l'idroconversione di prodotti petroliferi pesanti
IT1398288B1 (it) * 2009-09-30 2013-02-22 Eni Spa Ossidi misti di metalli di transizione, catalizzatori di idrotrattamento da essi ottenuti, e processo di preparazione comprendente procedimenti sol-gel
FI125931B (fi) * 2010-05-25 2016-04-15 Upm Kymmene Corp Menetelmä ja laitteisto hiilivetyjen valmistamiseksi
US8356678B2 (en) * 2010-10-29 2013-01-22 Racional Energy & Environment Company Oil recovery method and apparatus
ITMI20120685A1 (it) * 2012-04-24 2013-10-25 Eni Spa "ossidi misti di metalli di transizione, catalizzatori di idrotrattamento da essi ottenuti, e processo di preparazione comprendente procedimenti sol-gel"
FR2991063B1 (fr) * 2012-05-25 2016-12-09 Centre Scient Et Technique Du Batiment Ecran de projection courbe
US10537883B2 (en) 2016-10-07 2020-01-21 King Fahd University Of Petroleum And Minerals Method for producing a hydrodesulfurization catalyst
CN108435244B (zh) * 2018-03-20 2020-10-30 中海油天津化工研究设计院有限公司 一种提高十六烷值加氢改质催化剂、制备方法及其应用
CN112973712A (zh) * 2019-12-16 2021-06-18 北京中能炜业科技发展有限公司 加氢精制催化剂及其的制备方法

Family Cites Families (44)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US599439A (en) 1898-02-22 bennett
US3308069A (en) 1964-05-01 1967-03-07 Mobil Oil Corp Catalytic composition of a crystalline zeolite
US3536606A (en) * 1968-09-30 1970-10-27 Chevron Res Hydrocarbon conversion catalyst comprising an ultra-stable crystalline zeolitic molecular sieve component,and methods for making and using said catalyst
US4126579A (en) * 1977-03-22 1978-11-21 W. R. Grace & Co. Hydrocarbon conversion catalyst manufacture
US4299733A (en) * 1980-05-08 1981-11-10 Uop Inc. High octane FCC catalyst
US4343692A (en) 1981-03-27 1982-08-10 Shell Oil Company Catalytic dewaxing process
CA1203225A (fr) 1981-08-07 1986-04-15 Stephen M. Oleck Deparaffinage et hydrotraitement d'hydrocarbures en deux etapes
NZ204093A (en) * 1982-05-18 1985-01-31 Mobil Oil Corp Simultaneous catalytic hydrocracking and hydrodewaxing of hydrocarbon oils using zeolite beta
US4519900A (en) 1982-12-28 1985-05-28 Mobil Oil Corporation Zeolite containing catalyst support for denitrogenation of oil feedstocks
US4844792A (en) * 1984-08-07 1989-07-04 Union Oil Company Of California Hydroprocessing with a specific pore sized catalyst containing non-hydrolyzable halogen
US4568655A (en) * 1984-10-29 1986-02-04 Mobil Oil Corporation Catalyst composition comprising Zeolite Beta
AU4817385A (en) * 1984-10-29 1986-05-08 Mobil Oil Corporation Hydrotreating and dewaxing
US4913797A (en) * 1985-11-21 1990-04-03 Mobil Oil Corporation Catalyst hydrotreating and dewaxing process
US4959140A (en) 1989-03-27 1990-09-25 Amoco Corporation Two-catalyst hydrocracking process
US5011593A (en) * 1989-11-20 1991-04-30 Mobil Oil Corporation Catalytic hydrodesulfurization
US4996386A (en) 1989-12-21 1991-02-26 Shell Oil Company Concurrent isomerization and disproportionation of olefins
US5043520A (en) 1989-12-21 1991-08-27 Shell Oil Company Concurrent isomerization and disproportionation of olefins
US5120896A (en) 1989-12-21 1992-06-09 Shell Oil Company Concurrent isomerization and disproportionation of olefins
US5275720A (en) * 1990-11-30 1994-01-04 Union Oil Company Of California Gasoline hydrocracking catalyst and process
US5152885A (en) * 1990-12-18 1992-10-06 Exxon Research And Engineering Company Hydrotreating process using noble metal supported catalysts
US5362696A (en) * 1991-03-11 1994-11-08 Research Association For The Utilization Of Light Oil Process for producing spherical zeolite catalyst and apparatus for producing the same
US5298150A (en) 1991-08-15 1994-03-29 Mobil Oil Corporation Gasoline upgrading process
US5326462A (en) 1991-08-15 1994-07-05 Mobil Oil Corporation Gasoline upgrading process
US5510016A (en) 1991-08-15 1996-04-23 Mobil Oil Corporation Gasoline upgrading process
US5320742A (en) 1991-08-15 1994-06-14 Mobil Oil Corporation Gasoline upgrading process
US5500108A (en) 1991-08-15 1996-03-19 Mobil Oil Corporation Gasoline upgrading process
US5318690A (en) 1991-08-15 1994-06-07 Mobil Oil Corporation Gasoline upgrading process
US5360532A (en) 1991-08-15 1994-11-01 Mobil Oil Corporation Gasoline upgrading process
AU658937B2 (en) 1991-11-19 1995-05-04 Mobil Oil Corporation Hydrocarbon upgrading process
US5554274A (en) 1992-12-11 1996-09-10 Mobil Oil Corporation Manufacture of improved catalyst
RU2067023C1 (ru) * 1993-07-19 1996-09-27 Всероссийский научно-исследовательский институт по переработке нефти Способ получения катализатора для гидроочистки нефтяных фракций
US5800698A (en) * 1994-12-30 1998-09-01 Intevep, S.A. Catalyst for the hydroisomerization of contaminated hydrocarbon feedstock
IT1276726B1 (it) 1995-06-15 1997-11-03 Eniricerche Spa Gel di allumina mesoporoso e procedimento per la sua preparazione
US5865988A (en) * 1995-07-07 1999-02-02 Mobil Oil Corporation Hydrocarbon upgrading process
US5853566A (en) * 1995-11-28 1998-12-29 Shell Oil Company Zeolite-beta containing catalyst compositions and their use in hydrocarbon conversion processes for producing low boiling point materials
ES2167626T3 (es) * 1996-02-22 2002-05-16 Enichem Spa Materiales compuestos a base de silice y zeolita en forma esferica y procedimiento para su preparacion.
US5689026A (en) * 1996-04-24 1997-11-18 Phillips Petroleum Company Hydrodealkylation process
US5866744A (en) * 1997-01-30 1999-02-02 Phillips Petroleum Company Process for converting a c9 + hydrocarbon to a C6 to C8 aromatic using a steamed, acid-leached, impregnated zeolite
US5906729A (en) * 1997-12-08 1999-05-25 Mobil Oil Corporation Process scheme for processing sour feed in isomerization dewaxing
EP0955093B1 (fr) * 1998-05-06 2003-09-03 Institut Francais Du Petrole Catalyseur à base de zéolithe bêta et d'element promoteur et procédé d'hydrocraquage
ES2260892T3 (es) * 1998-06-25 2006-11-01 Institut Francais Du Petrole Catalizador de hidro craqueo que comprende una zeolita beta y un elemento del grupo vb.
RU2142339C1 (ru) * 1998-11-11 1999-12-10 Малое внедренческое предприятие ООО "Алкалит" Способ получения алюмооксидного катализатора подготовки сырья для гидрооблагораживания нефтяных фракций
IT1311512B1 (it) * 1999-03-12 2002-03-13 Agip Petroli Composizione catalitica per l'upgrading di miscele idrocarburiche.
EP1403358A1 (fr) 2002-09-27 2004-03-31 ENI S.p.A. Procédé et catalysateurs pour la désulfuration profonde de carburants

Also Published As

Publication number Publication date
US7754637B2 (en) 2010-07-13
ITMI990504A1 (it) 2000-09-12
EP1637224A2 (fr) 2006-03-22
AU2075100A (en) 2000-09-14
CN100374530C (zh) 2008-03-12
EP1637224A3 (fr) 2009-07-22
AU778458B2 (en) 2004-12-09
DE60025880D1 (de) 2006-04-20
DE60025880T2 (de) 2006-10-26
CA2300230C (fr) 2010-05-18
DK1034841T3 (da) 2006-06-26
EP1034841A2 (fr) 2000-09-13
US20070084756A1 (en) 2007-04-19
JP2000279816A (ja) 2000-10-10
ATE317296T1 (de) 2006-02-15
NO20001190D0 (no) 2000-03-08
PT1034841E (pt) 2006-06-30
IT1311512B1 (it) 2002-03-13
BR0001279A (pt) 2001-01-16
US7156980B2 (en) 2007-01-02
CN1276408A (zh) 2000-12-13
RU2245191C2 (ru) 2005-01-27
EP1034841A3 (fr) 2000-12-27
US6803337B1 (en) 2004-10-12
CA2300230A1 (fr) 2000-09-12
ES2257263T3 (es) 2006-08-01
US20040248726A1 (en) 2004-12-09
EP1034841B1 (fr) 2006-02-08

Similar Documents

Publication Publication Date Title
NO20001190D0 (no) Katalytisk blanding og fremgangsmÕte for fremstilling derav
JP4798324B2 (ja) 少なくとも３留分への分別により生じた重質フラクションおよび中間フラクションの脱硫を含むガソリンの脱硫方法
NO20002376D0 (no) Katalysatorsammensetning for oppgradering av hydrokarboner med kokepunkt i naftaomrÕdet
AU562743B2 (en) Zeolite catalytic dewaxing process
JP4547745B2 (ja) 低硫黄含有量のガソリンの製造方法
US5364514A (en) Hydrocarbon conversion process
CA2290693A1 (fr) Processus d'enrichissement des hydrocarbures
NO970362L (no) Fremgangsmåte for oppgradering av bensin
GB2289689A (en) Hydroprocessing scheme for production of premium isomerized light gasoline
NO20012406L (no) Fremgangsmåte for katalytisk avvoksing
US3816296A (en) Hydrocracking process
JP2010539253A (ja) ディーゼル沸点範囲原料の固体酸補助高度脱硫
CA2168720C (fr) Procede de desulfuration d'essence fractionnee par catalyse
JP2000239668A (ja) 低硫黄含有量のガソリン製造方法
GB1472655A (en) Process for producing lubricating oils
NO20010748L (no) Fremgangsmåte og katalysatorer for oppgradering av hydrokarboner som koker i naftaområdet
CA2339137A1 (fr) Catalyseur de zeolite de type l
JP4143411B2 (ja) 水素化処理されたフィッシャー・トロプシュ生成物の脱硫
EP1013339A3 (fr) Composition catalytique pour l'amélioration des hydrocarbures bouillant dans la plage d'ébullition du naphta
WO2016073394A1 (fr) Procédés de maximisation de distillat de haute qualité
EP0875287A3 (fr) Catalyseur d'hydrotraitement, sa préparation et procédé d'hydrotraitement d'huilse hydrocarbonées l'utilisant
KR100813775B1 (ko) 황 함량이 낮은 가솔린의 제조 방법
KR960037802A (ko) 접촉 분해된 가솔린의 탈황처리방법
CA1137909A (fr) Methode de preparation d'une alimentation de procede de craquage catalytique
JPH02152933A (ja) 高品質イソパラフィンの製法

Legal Events

Date Code Title Description
FC2A Withdrawal, rejection or dismissal of laid open patent application