NO20090743L - Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of distillate - Google Patents

Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of distillate

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
Norwegian (no)
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/en

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.Increased selectivity of intermediate distillate and increased catalyst activity is achieved in a hydrocracking process using a catalyst containing a hydrogenation component, a beta zeolite having a total molar ratio of silica and alumina lower than 30, and an SF6 adsorption capacity of at least 28% by weight, a Y zeolite with a unit cell size of from 24.25 to 24.32 angstroms and a carrier.

NO20090743A 2006-07-17 2009-02-16 Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of distillate NO20090743L (en)

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 (en) 2009-02-16

Family

ID=38948160

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20090743A NO20090743L (en) 2006-07-17 2009-02-16 Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of distillate

Country Status (11)

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

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009545441A (en) * 2006-07-31 2009-12-24 シェブロン ユー．エス．エー． インコーポレイテッド Hydrotreating catalyst and usage
KR20100014272A (en) * 2007-01-12 2010-02-10 유오피 엘엘씨 Selective hydrocracking process using beta zeolite
US8105969B2 (en) * 2008-12-29 2012-01-31 Fina Technology Inc. Catalyst with an ion-modified binder
RU2612973C2 (en) * 2012-09-13 2017-03-14 Басф Корпорейшн Novel catalyst to increase propylene yields from 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
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
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

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 (en) * 2000-10-26 2003-05-14 中国石油化工股份有限公司 High-activity high-or medium-oilness hydrocracking catalyst and its preparing process
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
BRPI0508276A (en) * 2004-03-03 2007-08-07 Shell Int Research shaped catalytic support, process for preparing a catalytic support, catalytic composition, processes for preparing a catalytic and hydrocracking composition, and, use of a catalytic composition
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
WO2008011291A2 (en) 2008-01-24
EP2041244A2 (en) 2009-04-01
AU2007275504A1 (en) 2008-01-24
CA2657313A1 (en) 2008-01-24
MX2009000438A (en) 2009-01-29
CN101490217A (en) 2009-07-22
WO2008011291A3 (en) 2008-03-20
CL2007002042A1 (en) 2008-02-01
KR20090025364A (en) 2009-03-10
RU2009105256A (en) 2010-08-27
US20080011648A1 (en) 2008-01-17

Similar Documents

Publication Publication Date Title
NO20090743L (en) Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of distillate
NO20082492L (en) Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of naphtha
NO20082495L (en) Hydrocracking catalyst containing beta and Y zeolites and process for their use in the production of jet fuel or distillate
WO2009105344A3 (en) Production of aromatics from methane
MY167567A (en) A modified y-type zeolite and preparation process and use thereof
JP2012143751A5 (en)
RU2008114834A (en) METHOD FOR PRODUCING ETHYLENE AND PROPYLENE
CA2796341A1 (en) Xylene isomerization process and catalyst therefor
JP2011530397A5 (en)
NO20090742L (en) Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of distillate
WO2009097067A3 (en) Production of aromatics from methane
IN2012DN00751A (en)
CN102671622A (en) Combined adsorbent, preparation method thereof and method for removing and recycling thiophene by using combined adsorbent
EP1839747A3 (en) Adsorbent for hydrocarbons, catalyst for exhaust gas purification and method for exhaust gas purification
RU2015144970A (en) HYDRODESULFURIZATION CATALYST FOR DIESEL FUEL AND DIESEL FUEL HYDROCLEANING METHOD
FI20085366L (en) Catalytic cracking of hydrocarbons
CN101982232B (en) Deaminizing agent and preparation method thereof
Zhang et al. Isolated zinc in mordenite stabilizing carbonylation of dimethyl ether to methyl acetate
ZA200109075B (en) Zeolite bound catalyst containing at least three different zeolites; use for hydrocarbon conversion.
DE60309707D1 (en) USE OF A ZEOLITE BETA-CONTAINING CATALYST IN HYDROCARBONOUND REVERSE PROCESSES
TW200728266A (en) Method for producing ethylene and propylene
NO20090647L (en) Hydrocracking catalyst containing beta and Y zeolites and process for its use in the preparation of distillate
WO2010005859A3 (en) Processes for hydrogenation
CL2008001772A1 (en) Process for the preparation of melamine by decomposition of urea by using a catalyst comprising 10-90% by weight of zeolite, 10-90% of a matrix containing silica, alumina, silicon and aluminum oxides, 0-10% of additives and the content of nickel and vanadium is less than 500 ppm; and catalyst.
JP2000024509A5 (en)

Legal Events

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