CL2007002040A1 - COMPOSITION OF MATERIAL THAT INCLUDES CATALYZER CONTAINING HYDROGENATION COMPONENT, ZEOLITA BETA (Z1) WITH TOTAL MOLAR REASON SIO2 / AL2O3 <30, ZEOLITA YI (Z2) OF SIZE 24,25-24,32 A AND MOLAR REASON SIO2 / AL2 5-11 , CATALYST CONTAINS 0.1-2% IN P - Google Patents

COMPOSITION OF MATERIAL THAT INCLUDES CATALYZER CONTAINING HYDROGENATION COMPONENT, ZEOLITA BETA (Z1) WITH TOTAL MOLAR REASON SIO2 / AL2O3 <30, ZEOLITA YI (Z2) OF SIZE 24,25-24,32 A AND MOLAR REASON SIO2 / AL2 5-11 , CATALYST CONTAINS 0.1-2% IN P

Info

Publication number
CL2007002040A1
CL2007002040A1 CL200702040A CL2007002040A CL2007002040A1 CL 2007002040 A1 CL2007002040 A1 CL 2007002040A1 CL 200702040 A CL200702040 A CL 200702040A CL 2007002040 A CL2007002040 A CL 2007002040A CL 2007002040 A1 CL2007002040 A1 CL 2007002040A1
Authority
CL
Chile
Prior art keywords
zeolita
sio2
molar reason
reason
al2o3
Prior art date
Application number
CL200702040A
Other languages
Spanish (es)
Inventor
Wang Li
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 CL2007002040A1 publication Critical patent/CL2007002040A1/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
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
CL200702040A 2006-07-17 2007-07-13 COMPOSITION OF MATERIAL THAT INCLUDES CATALYZER CONTAINING HYDROGENATION COMPONENT, ZEOLITA BETA (Z1) WITH TOTAL MOLAR REASON SIO2 / AL2O3 <30, ZEOLITA YI (Z2) OF SIZE 24,25-24,32 A AND MOLAR REASON SIO2 / AL2 5-11 , CATALYST CONTAINS 0.1-2% IN P CL2007002040A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US11/457,824 US20080011647A1 (en) 2006-07-17 2006-07-17 Hydrocracking Catalyst Containing Beta and Y Zeolites, and Process for its use to make Distillate

Publications (1)

Publication Number Publication Date
CL2007002040A1 true CL2007002040A1 (en) 2008-02-29

Family

ID=38948159

Family Applications (1)

Application Number Title Priority Date Filing Date
CL200702040A CL2007002040A1 (en) 2006-07-17 2007-07-13 COMPOSITION OF MATERIAL THAT INCLUDES CATALYZER CONTAINING HYDROGENATION COMPONENT, ZEOLITA BETA (Z1) WITH TOTAL MOLAR REASON SIO2 / AL2O3 <30, ZEOLITA YI (Z2) OF SIZE 24,25-24,32 A AND MOLAR REASON SIO2 / AL2 5-11 , CATALYST CONTAINS 0.1-2% IN P

Country Status (13)

Country Link
US (1) US20080011647A1 (en)
EP (1) EP2041243A2 (en)
JP (1) JP2009543692A (en)
KR (1) KR20090031773A (en)
CN (1) CN101516505A (en)
AU (1) AU2007275501A1 (en)
CA (1) CA2657632A1 (en)
CL (1) CL2007002040A1 (en)
CO (1) CO6190562A2 (en)
MX (1) MX2009000566A (en)
NO (1) NO20090647L (en)
RU (1) RU2009105257A (en)
WO (1) WO2008011288A2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2115100A4 (en) * 2007-01-12 2012-12-05 Uop Llc Selective hydrocracking process using beta zeolite
CN102765732A (en) * 2011-05-06 2012-11-07 天津神能科技有限公司 Preparation method of Y with high silica-alumina ratio
RU2697711C1 (en) * 2019-02-13 2019-08-19 Федеральное государственное бюджетное учреждение науки "Федеральный исследовательский центр "Институт катализа им. Г.К. Борескова Сибирского отделения Российской академии наук" (ИК СО РАН) Method of preparing a catalyst and method for hydrocracking of vacuum gas oil using said catalyst

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4563434A (en) * 1982-08-09 1986-01-07 Union Oil Company Of California Hydrocracking catalyst
US4914067A (en) * 1983-05-02 1990-04-03 Uop Catalytic cracking catalysts and cracking process using mixed catalyst system
US4486296A (en) * 1983-10-13 1984-12-04 Mobil Oil Corporation Process for hydrocracking and dewaxing hydrocarbon oils
US4661239A (en) * 1985-07-02 1987-04-28 Uop Inc. Middle distillate producing hydrocracking process
US4764266A (en) * 1987-02-26 1988-08-16 Mobil Oil Corporation Integrated hydroprocessing scheme for production of premium quality distillates and lubricants
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
TW252053B (en) * 1991-11-01 1995-07-21 Shell Internat Res Schappej Bv
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
US6699811B1 (en) * 1999-05-05 2004-03-02 Exxon Mobil Chemical Patents Inc. Tailored zeolite bound zeolite catalyst and its use for hydrocarbon conversion
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
CN1839195A (en) * 2003-06-26 2006-09-27 赫多特普索化工设备公司 Hydrocarbon conversion process and catalyst
CN100428995C (en) * 2004-03-03 2008-10-29 国际壳牌研究有限公司 Catalyst carrier and catalyst composition, processes for their preparation and their use
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
WO2008011288A3 (en) 2008-03-13
AU2007275501A1 (en) 2008-01-24
EP2041243A2 (en) 2009-04-01
WO2008011288A2 (en) 2008-01-24
RU2009105257A (en) 2010-08-27
KR20090031773A (en) 2009-03-27
MX2009000566A (en) 2009-01-29
JP2009543692A (en) 2009-12-10
CA2657632A1 (en) 2008-01-24
CN101516505A (en) 2009-08-26
NO20090647L (en) 2009-02-10
CO6190562A2 (en) 2010-08-19
US20080011647A1 (en) 2008-01-17

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