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 distillateInfo
- 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
Links
- 239000003054 catalyst Substances 0.000 title abstract 3
- 239000010457 zeolite Substances 0.000 title abstract 3
- 238000004517 catalytic hydrocracking Methods 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 2
- 229910021536 Zeolite Inorganic materials 0.000 abstract 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 230000000694 effects Effects 0.000 abstract 1
- 238000005984 hydrogenation reaction Methods 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- 238000001179 sorption measurement Methods 0.000 abstract 1
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)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (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.
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)
| 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 |
| 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 |
| 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)
| 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 |
| JP2007526119A (en) * | 2004-03-03 | 2007-09-13 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | Catalyst support and catalyst composition, method for their preparation and method for their use |
| US7611689B2 (en) * | 2004-09-24 | 2009-11-03 | Shell Oil Company | Faujasite zeolite, its preparation and use in hydrocracking |
-
2006
- 2006-07-17 US US11/457,833 patent/US20080011648A1/en not_active Abandoned
-
2007
- 2007-07-09 AU AU2007275504A patent/AU2007275504A1/en not_active Abandoned
- 2007-07-09 RU RU2009105256/04A patent/RU2009105256A/en unknown
- 2007-07-09 WO PCT/US2007/073051 patent/WO2008011291A2/en not_active Ceased
- 2007-07-09 EP EP07799400A patent/EP2041244A2/en not_active Withdrawn
- 2007-07-09 MX MX2009000438A patent/MX2009000438A/en unknown
- 2007-07-09 CN CNA2007800271976A patent/CN101490217A/en active Pending
- 2007-07-09 KR KR1020097001591A patent/KR20090025364A/en not_active Ceased
- 2007-07-09 CA CA002657313A patent/CA2657313A1/en not_active Abandoned
- 2007-07-13 CL CL200702042A patent/CL2007002042A1/en unknown
-
2009
- 2009-02-16 NO NO20090743A patent/NO20090743L/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| RU2009105256A (en) | 2010-08-27 |
| US20080011648A1 (en) | 2008-01-17 |
| CN101490217A (en) | 2009-07-22 |
| WO2008011291A3 (en) | 2008-03-20 |
| AU2007275504A1 (en) | 2008-01-24 |
| CA2657313A1 (en) | 2008-01-24 |
| KR20090025364A (en) | 2009-03-10 |
| MX2009000438A (en) | 2009-01-29 |
| EP2041244A2 (en) | 2009-04-01 |
| CL2007002042A1 (en) | 2008-02-01 |
| WO2008011291A2 (en) | 2008-01-24 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FC2A | Withdrawal, rejection or dismissal of laid open patent application |