CO6190562A2 - Catalizador de craneo con hidrogeno que contiene zeolitas beta y zeolitas-y y proceso para su uso en la elaboracion de destilado - Google Patents
Catalizador de craneo con hidrogeno que contiene zeolitas beta y zeolitas-y y proceso para su uso en la elaboracion de destiladoInfo
- Publication number
- CO6190562A2 CO6190562A2 CO09011072A CO09011072A CO6190562A2 CO 6190562 A2 CO6190562 A2 CO 6190562A2 CO 09011072 A CO09011072 A CO 09011072A CO 09011072 A CO09011072 A CO 09011072A CO 6190562 A2 CO6190562 A2 CO 6190562A2
- Authority
- CO
- Colombia
- Prior art keywords
- zeolite
- catalyst
- weight
- beta
- unit cell
- Prior art date
Links
- 239000010457 zeolite Substances 0.000 title abstract 9
- 239000003054 catalyst Substances 0.000 title abstract 7
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title abstract 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical class [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title 1
- 238000009395 breeding Methods 0.000 title 1
- 230000001488 breeding effect Effects 0.000 title 1
- 238000004821 distillation Methods 0.000 title 1
- 229910052739 hydrogen Inorganic materials 0.000 title 1
- 239000001257 hydrogen Substances 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- 229910021536 Zeolite Inorganic materials 0.000 abstract 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-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 2
- 238000005984 hydrogenation reaction Methods 0.000 abstract 2
- 239000000377 silicon dioxide Substances 0.000 abstract 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 abstract 1
- 239000010941 cobalt Substances 0.000 abstract 1
- 229910017052 cobalt Inorganic materials 0.000 abstract 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 229910052750 molybdenum Inorganic materials 0.000 abstract 1
- 239000011733 molybdenum Substances 0.000 abstract 1
- 229910052759 nickel Inorganic materials 0.000 abstract 1
- 238000001179 sorption measurement Methods 0.000 abstract 1
- 150000003568 thioethers Chemical class 0.000 abstract 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 abstract 1
- 229910052721 tungsten Inorganic materials 0.000 abstract 1
- 239000010937 tungsten Substances 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
-
- 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)
Abstract
1.- Una composición de material que comprende un catalizador conformado por un soporte, componente de hidrogenación, una zeolita Beta con una relación molar total de sílice a alúmina menor de 30 y una capacidad de adsorción de SF6 de por lo menos 28% en peso, donde el catalizador además comprende: a. una primera zeolita-Y con un tamaño de celda unitaria desde 24.25 a 24.32 angstroms (Zeolita-Y I). b. una segunda zeolita-Y con un tamaño de celda unitaria desde 24.33 a 24.38 angstroms (Zeolita-Y II), donde, i. el tamaño de celda unitaria de la zeolita-Y II es al menos 0.04 angstrom mayor que el tamaño de celda unitaria de la zeolita-Y I.ii. el catalizador tiene una relación de peso de la zeolita-Y I a la zeolita-Y II de 1.5 a 6.5 sobre una base seca, iii. el catalizador tiene una cantidad positiva de máximo 5% en peso de la zeolita-Y I y la zeolita-Y II basado en el peso combinado de la zeolita Beta, la zeolita-Y II, la zeolita-Y II y el soporte; en donde la zeolita-Y I tiene una relación molar total de sílice a alúmina de 5.0 a 11.0, en donde el catalizador contiene desde 0.1 a 2% en peso de zeolita Beta basado en el peso combinado de la zeolita Beta, la zeolita-Y I, la zeolita-Y II y el soporte sobre una base seca, y en donde el catalizador tiene una relación de peso de la zeolita-Y I a la zeolita Beta de 1 a 10 sobre una base seca. 2.- La composición de la reivindicación 1 en donde la zeolita-Y I tiene un área superficial menor de 800 m2/g. 3.- La composición de la reivindicación 1 en donde el componente de hidrogenación se selecciona del grupo conformado por molibdeno, tungsteno, níquel, cobalto y los óxidos y sulfuros de los mismos.
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 |
|---|---|
| CO6190562A2 true CO6190562A2 (es) | 2010-08-19 |
Family
ID=38948159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CO09011072A CO6190562A2 (es) | 2006-07-17 | 2009-02-05 | Catalizador de craneo con hidrogeno que contiene zeolitas beta y zeolitas-y y proceso para su uso en la elaboracion de destilado |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US20080011647A1 (es) |
| EP (1) | EP2041243A2 (es) |
| JP (1) | JP2009543692A (es) |
| KR (1) | KR20090031773A (es) |
| CN (1) | CN101516505A (es) |
| AU (1) | AU2007275501A1 (es) |
| CA (1) | CA2657632A1 (es) |
| CL (1) | CL2007002040A1 (es) |
| CO (1) | CO6190562A2 (es) |
| MX (1) | MX2009000566A (es) |
| NO (1) | NO20090647L (es) |
| RU (1) | RU2009105257A (es) |
| WO (1) | WO2008011288A2 (es) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101578353B (zh) * | 2007-01-12 | 2013-01-16 | 环球油品公司 | 利用β沸石选择性的氢化裂化的方法 |
| CN102765732A (zh) * | 2011-05-06 | 2012-11-07 | 天津神能科技有限公司 | 一种高硅铝比y的制备方法 |
| RU2697711C1 (ru) * | 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) | Способ приготовления катализатора и способ гидрокрекинга вакуумного гайзоля с использованием этого катализатора |
Family Cites Families (19)
| 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 (es) * | 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 (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 |
| KR20060023175A (ko) * | 2003-06-26 | 2006-03-13 | 할도르 토프쉐 에이/에스 | 탄화수소 전환 공정 및 촉매 |
| US20050197249A1 (en) * | 2004-03-03 | 2005-09-08 | Creyghton Edward J. | 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 |
-
2006
- 2006-07-17 US US11/457,824 patent/US20080011647A1/en not_active Abandoned
-
2007
- 2007-07-09 KR KR1020097002987A patent/KR20090031773A/ko not_active Application Discontinuation
- 2007-07-09 MX MX2009000566A patent/MX2009000566A/es unknown
- 2007-07-09 RU RU2009105257/04A patent/RU2009105257A/ru unknown
- 2007-07-09 CA CA002657632A patent/CA2657632A1/en not_active Abandoned
- 2007-07-09 EP EP07812720A patent/EP2041243A2/en not_active Withdrawn
- 2007-07-09 AU AU2007275501A patent/AU2007275501A1/en not_active Abandoned
- 2007-07-09 JP JP2009520887A patent/JP2009543692A/ja not_active Withdrawn
- 2007-07-09 CN CNA2007800343866A patent/CN101516505A/zh active Pending
- 2007-07-09 WO PCT/US2007/073031 patent/WO2008011288A2/en active Application Filing
- 2007-07-13 CL CL200702040A patent/CL2007002040A1/es unknown
-
2009
- 2009-02-05 CO CO09011072A patent/CO6190562A2/es not_active Application Discontinuation
- 2009-02-10 NO NO20090647A patent/NO20090647L/no not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| CL2007002040A1 (es) | 2008-02-29 |
| MX2009000566A (es) | 2009-01-29 |
| WO2008011288A2 (en) | 2008-01-24 |
| NO20090647L (no) | 2009-02-10 |
| CN101516505A (zh) | 2009-08-26 |
| US20080011647A1 (en) | 2008-01-17 |
| KR20090031773A (ko) | 2009-03-27 |
| WO2008011288A3 (en) | 2008-03-13 |
| EP2041243A2 (en) | 2009-04-01 |
| JP2009543692A (ja) | 2009-12-10 |
| RU2009105257A (ru) | 2010-08-27 |
| CA2657632A1 (en) | 2008-01-24 |
| AU2007275501A1 (en) | 2008-01-24 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FA | Application withdrawn |