NO20090743L - Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av destillat - Google Patents

Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av destillat

Info

Publication number
NO20090743L
NO20090743L NO20090743A NO20090743A NO20090743L NO 20090743 L NO20090743 L NO 20090743L NO 20090743 A NO20090743 A NO 20090743A NO 20090743 A NO20090743 A NO 20090743A NO 20090743 L NO20090743 L NO 20090743L
Authority
NO
Norway
Prior art keywords
catalyst containing
distillate
zeolites
preparation
hydrocracking catalyst
Prior art date
Application number
NO20090743A
Other languages
English (en)
Inventor
Li Wang
Original Assignee
Uop Llc
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 Uop Llc filed Critical Uop Llc
Publication of NO20090743L publication Critical patent/NO20090743L/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
    • 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
    • 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
    • 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
    • B01J23/28—Molybdenum
    • 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
    • B01J23/30—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
    • B01J23/75—Cobalt
    • 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
    • B01J23/755—Nickel
    • 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
    • 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
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084—Y-type faujasite
    • 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
    • B01J29/7007—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
    • 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
    • B01J29/80—Mixtures of different 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
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/653—500-1000 nm
    • 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
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Øket selektivitet av mellomdestillat og øket katalysatoraktivitet oppnås i en hydrokrakkingprosess ved bruk av en katalysator inneholdende en hydrogeneringskomponent, en beta-zeolitt med et totalt molforhold mellom silika og alumina lavere enn 30 og en SF6-adsorpsjonskapasitet på minst 28 vekt%, en Y-zeolitt med en enhetscellestørrelse på fra 24,25 til 24,32 ångstrøm og en bærer.
NO20090743A 2006-07-17 2009-02-16 Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av destillat NO20090743L (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US11/457,833 US20080011648A1 (en) 2006-07-17 2006-07-17 Hydrocracking Catalyst Containing Beta and Y Zeolites, and Process for its use to make Distillate
PCT/US2007/073051 WO2008011291A2 (en) 2006-07-17 2007-07-09 Hydrocracking catalyst containing beta and y zeolites, and process for its use to make distillate

Publications (1)

Publication Number Publication Date
NO20090743L true NO20090743L (no) 2009-02-16

Family

ID=38948160

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20090743A NO20090743L (no) 2006-07-17 2009-02-16 Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av destillat

Country Status (11)

Country Link
US (1) US20080011648A1 (no)
EP (1) EP2041244A2 (no)
KR (1) KR20090025364A (no)
CN (1) CN101490217A (no)
AU (1) AU2007275504A1 (no)
CA (1) CA2657313A1 (no)
CL (1) CL2007002042A1 (no)
MX (1) MX2009000438A (no)
NO (1) NO20090743L (no)
RU (1) RU2009105256A (no)
WO (1) WO2008011291A2 (no)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008016888A2 (en) * 2006-07-31 2008-02-07 Chevron U.S.A. Inc. Hydroprocessing catalyst and process of use
WO2008085517A1 (en) * 2007-01-12 2008-07-17 Uop Llc Selective hydrocracking process using beta zeolite
US8105969B2 (en) * 2008-12-29 2012-01-31 Fina Technology Inc. Catalyst with an ion-modified binder
WO2014042641A1 (en) * 2012-09-13 2014-03-20 Basf Corporation Novel catalyst to increase propylene yields from a fluid catalytic cracking unit
US10046317B2 (en) * 2015-08-11 2018-08-14 Chevron U.S.A. Inc. Middle distillate hydrocracking catalyst containing zeolite beta with low OD acidity and large domain size
US10040058B2 (en) 2015-08-11 2018-08-07 Chevron U.S.A. Inc. Middle distillate hydrocracking catalyst containing zeolite USY, and zeolite beta with low acidity and large domain size
US10183286B2 (en) 2015-08-11 2019-01-22 Chevron U.S.A. Inc. Noble metal zeolite catalyst for second-stage hydrocracking to make middle distillate

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4486296A (en) * 1983-10-13 1984-12-04 Mobil Oil Corporation Process for hydrocracking and dewaxing hydrocarbon oils
US4604373A (en) * 1984-08-24 1986-08-05 Union Oil Company Of California Hydrocracking catalyst of improved activity
US4661239A (en) * 1985-07-02 1987-04-28 Uop Inc. Middle distillate producing hydrocracking process
US5160033A (en) * 1988-03-30 1992-11-03 Uop Octane gasoline catalyst and process using same in a hydrocracking process
US4925546A (en) * 1989-09-12 1990-05-15 Amoco Corporation Hydrocracking process
US5350501A (en) * 1990-05-22 1994-09-27 Union Oil Company Of California Hydrocracking catalyst and process
US5279726A (en) * 1990-05-22 1994-01-18 Union Oil Company Of California Catalyst containing zeolite beta and processes for its use
US5275720A (en) * 1990-11-30 1994-01-04 Union Oil Company Of California Gasoline hydrocracking catalyst and 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
CN1108356C (zh) * 2000-10-26 2003-05-14 中国石油化工股份有限公司 一种高活性高中油性加氢裂化催化剂及其制备方法
US7048845B2 (en) * 2001-11-07 2006-05-23 Uop Llc Middle distillate selective hydrocracking process
US7192900B2 (en) * 2002-11-27 2007-03-20 Shell Oil Company Hydrocracking catalyst
KR20070004776A (ko) * 2004-03-03 2007-01-09 쉘 인터내셔날 리써취 마트샤피지 비.브이. 촉매 담체 및 촉매 조성물, 그의 제조 방법 및 그의 용도
US7611689B2 (en) * 2004-09-24 2009-11-03 Shell Oil Company Faujasite zeolite, its preparation and use in hydrocracking

Also Published As

Publication number Publication date
EP2041244A2 (en) 2009-04-01
AU2007275504A1 (en) 2008-01-24
CA2657313A1 (en) 2008-01-24
WO2008011291A2 (en) 2008-01-24
RU2009105256A (ru) 2010-08-27
CN101490217A (zh) 2009-07-22
WO2008011291A3 (en) 2008-03-20
KR20090025364A (ko) 2009-03-10
MX2009000438A (es) 2009-01-29
CL2007002042A1 (es) 2008-02-01
US20080011648A1 (en) 2008-01-17

Similar Documents

Publication Publication Date Title
NO20090743L (no) Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av destillat
NO20082492L (no) Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av nafta
NO20082495L (no) Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for deres anvendelse for fremstilling av jetbrennstoff eller destillat
EP2364213A4 (en) CHABAZITE-ZEOLITE CATALYSTS WITH SMALL SILICONE OXIDE-ALUMINUM OXIDE RATIO
MY167567A (en) A modified y-type zeolite and preparation process and use thereof
JP2012143751A5 (no)
CA2796341A1 (en) Xylene isomerization process and catalyst therefor
NO20090742L (no) Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av destillat
WO2009097067A3 (en) Production of aromatics from methane
WO2011041184A3 (en) Production of aromatics from methane
IN2012DN00751A (no)
RU2015144970A (ru) Катализатор гидродесульфуризации для дизельного топлива и способ гидроочистки дизельного топлива
FI20085366A0 (fi) Hiilivetyjen katalyyttinen krakkaus
RU2012126636A (ru) Способ конверсии парафинового сырья
IN2012DN02312A (no)
DE60309707D1 (de) Verwendung eines zeolith beta enthaltender katalysators in kohlenwasserstoffumwandlungsverfahren
MY145615A (en) Method for producing ethylene and propylene
NO20090647L (no) Hydrokrakkingkatalysator inneholdende beta- og Y-zeolitter og fremgangsmate for dens anvendelse for fremstilling av destillat
CN102091650B (zh) 一种草酸酯加氢铜硅催化剂及其制备方法
WO2010005859A3 (en) Processes for hydrogenation
JP2000024509A5 (no)
WO2008088962A8 (en) Y-85 and modified lz-210 zeolites
Su et al. From waste to best: excellent desulfurization performance of spent FCC catalyst
WO2007006924A8 (fr) Utilisation d'un catalyseur d'ouverture de cycles hydrocarbones
Qu et al. Studies on NO activity decomposed by Cu-ZSM-5 catalysts modified with rare earth Ce super (3+)(La super (3+))

Legal Events

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