ATE440931T1 - Verwendung eines katalysators zum hydrocracken bestehend aus einem mikroporísen kristallinen feststoff - Google Patents

Verwendung eines katalysators zum hydrocracken bestehend aus einem mikroporísen kristallinen feststoff

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Publication number
ATE440931T1
ATE440931T1 AT03765121T AT03765121T ATE440931T1 AT E440931 T1 ATE440931 T1 AT E440931T1 AT 03765121 T AT03765121 T AT 03765121T AT 03765121 T AT03765121 T AT 03765121T AT E440931 T1 ATE440931 T1 AT E440931T1
Authority
AT
Austria
Prior art keywords
crystalline solid
oxide
microporous crystalline
hydrocacking
calcined
Prior art date
Application number
AT03765121T
Other languages
German (de)
English (en)
Inventor
Canos Avelino Corma
Feliu A Martinez
Garcia F Rey
Cabanas M J Diaz
Pez Cruz Carlos L
Original Assignee
Consejo Superior Investigacion
Univ Valencia Politecnica
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 Consejo Superior Investigacion, Univ Valencia Politecnica filed Critical Consejo Superior Investigacion
Application granted granted Critical
Publication of ATE440931T1 publication Critical patent/ATE440931T1/de

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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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking 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
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • C10G47/18—Crystalline alumino-silicate carriers the catalyst 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts 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
    • B01J23/84—Catalysts 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
    • B01J23/85—Chromium, molybdenum or tungsten
    • 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
    • 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
    • B01J35/19—Catalysts containing parts with different compositions
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/04—Oxides
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking 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
    • C10G47/12—Inorganic carriers
    • C10G47/14—Inorganic carriers the catalyst containing platinum group 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking 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
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking 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
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other 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
    • 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
    • B01J2229/42—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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24—Chromium, molybdenum or tungsten
    • 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
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/20—Sulfiding

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
AT03765121T 2002-07-16 2003-07-15 Verwendung eines katalysators zum hydrocracken bestehend aus einem mikroporísen kristallinen feststoff ATE440931T1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ES200201753A ES2200701B1 (es) 2002-07-16 2002-07-16 Catalizador de hidrocraqueo conteniendo un material solido cristalino microporoso y uso de dicho catalizador para el hidrocraqueo de alimentacion de hidrocarburos.
PCT/ES2003/000367 WO2004009736A1 (es) 2002-07-16 2003-07-15 Catalizador de hidrocraqueo que comprende un material sólido cristalino microporoso

Publications (1)

Publication Number Publication Date
ATE440931T1 true ATE440931T1 (de) 2009-09-15

Family

ID=30470585

Family Applications (1)

Application Number Title Priority Date Filing Date
AT03765121T ATE440931T1 (de) 2002-07-16 2003-07-15 Verwendung eines katalysators zum hydrocracken bestehend aus einem mikroporísen kristallinen feststoff

Country Status (9)

Country Link
EP (1) EP1535983B1 (cg-RX-API-DMAC10.html)
JP (1) JP4676760B2 (cg-RX-API-DMAC10.html)
AT (1) ATE440931T1 (cg-RX-API-DMAC10.html)
AU (1) AU2003250254A1 (cg-RX-API-DMAC10.html)
CA (1) CA2492516C (cg-RX-API-DMAC10.html)
DE (1) DE60328999D1 (cg-RX-API-DMAC10.html)
DK (1) DK1535983T3 (cg-RX-API-DMAC10.html)
ES (1) ES2200701B1 (cg-RX-API-DMAC10.html)
WO (1) WO2004009736A1 (cg-RX-API-DMAC10.html)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2303449B1 (es) * 2006-08-01 2009-06-22 Universidad Politecnica De Valencia Hidrocraqueo de compuestos organicos utilizando la zeolita itq-33.
FR2963360B1 (fr) * 2010-07-29 2012-07-27 IFP Energies Nouvelles Procede d'hydrocraquage d'une charge hydrocarbonnee en presence d'un catalyseur sulfure prepare au moyen d'un oligosaccharide cyclique
FR2963358B1 (fr) 2010-07-29 2012-07-27 IFP Energies Nouvelles Procede d'hydrodesulfuration d'une coupe essence en presence d'un catalyseur sulfure supporte prepare au moyen d'au moins un oligosaccharide cyclique
CN102861601B (zh) * 2011-07-07 2015-08-26 中国石油化工股份有限公司 一种含氟的加氢催化剂及其制备
FR2981066B1 (fr) 2011-10-11 2015-04-17 Total Raffinage Marketing Procede de preparation de jet fuel a partir de molecules issues de la biomasse.
RU2742031C1 (ru) * 2019-10-03 2021-02-01 Публичное акционерное общество "Нефтяная компания "Роснефть" (ПАО "НК "Роснефть") Состав и способ приготовления катализатора - ловушки кремния
CN113731475A (zh) * 2020-05-27 2021-12-03 中国石油天然气股份有限公司 一种加氢裂化催化剂及其制备方法与应用
CN111686787B (zh) * 2020-06-10 2023-10-03 中国石油天然气集团有限公司 加氢裂化催化剂载体及其制备方法与应用
CN111672534B (zh) * 2020-06-10 2023-10-03 中国石油天然气集团有限公司 加氢裂化催化剂及其制备方法与应用
CN112973718B (zh) * 2021-02-22 2022-10-25 安徽工业大学 一种煤油共加氢催化剂及其制备方法

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4959140A (en) * 1989-03-27 1990-09-25 Amoco Corporation Two-catalyst hydrocracking process
US5219814A (en) * 1990-12-19 1993-06-15 Mobil Oil Corporation Catalyst for light cycle oil upgrading
WO1998000235A1 (fr) * 1996-06-28 1998-01-08 China Petrochemical Corporation Catalyseur d'hydrocraquage pour distillat d'huile et procede de production correspondant
FR2769856B1 (fr) * 1997-10-20 1999-12-03 Inst Francais Du Petrole Catalyseur et procede d'hydrocraquage de coupes hydrocarbonees
ES2192935B1 (es) * 2001-05-14 2004-08-16 Universidad Politecnica De Valencia Sintesis de zeolita itq-21.
ES2195744B1 (es) * 2001-10-04 2005-02-16 Universidad Politecnica De Valencia Aplicacion de la zeolita itq-21 en craqueo catalitico de hidrocarburos.

Also Published As

Publication number Publication date
ES2200701B1 (es) 2005-05-01
DK1535983T3 (da) 2009-12-07
CA2492516A1 (en) 2004-01-29
JP4676760B2 (ja) 2011-04-27
DE60328999D1 (de) 2009-10-08
WO2004009736A1 (es) 2004-01-29
CA2492516C (en) 2012-05-22
EP1535983B1 (en) 2009-08-26
ES2200701A1 (es) 2004-03-01
JP2005532905A (ja) 2005-11-04
AU2003250254A8 (en) 2004-02-09
AU2003250254A1 (en) 2004-02-09
EP1535983A1 (en) 2005-06-01

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