RU2017118406A - Катализатор гидрокрекинга средних дистиллятов, содержащий высокостабилизированный цеолит y с улучшенным распределением кислотных центров - Google Patents
Катализатор гидрокрекинга средних дистиллятов, содержащий высокостабилизированный цеолит y с улучшенным распределением кислотных центров Download PDFInfo
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- RU2017118406A RU2017118406A RU2017118406A RU2017118406A RU2017118406A RU 2017118406 A RU2017118406 A RU 2017118406A RU 2017118406 A RU2017118406 A RU 2017118406A RU 2017118406 A RU2017118406 A RU 2017118406A RU 2017118406 A RU2017118406 A RU 2017118406A
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- Prior art keywords
- nanopores
- stabilized zeolite
- hydrocracking
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- index
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- 229910021536 Zeolite Inorganic materials 0.000 title claims 11
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims 11
- 239000010457 zeolite Substances 0.000 title claims 11
- 239000003054 catalyst Substances 0.000 title claims 10
- 238000004517 catalytic hydrocracking Methods 0.000 title claims 8
- 239000002253 acid Substances 0.000 title claims 7
- 238000000034 method Methods 0.000 claims 8
- 239000011959 amorphous silica alumina Substances 0.000 claims 2
- 239000000463 material Substances 0.000 claims 2
- 239000002184 metal Substances 0.000 claims 2
- 230000000737 periodic effect Effects 0.000 claims 2
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- 229930195733 hydrocarbon Natural products 0.000 claims 1
- 150000002430 hydrocarbons Chemical class 0.000 claims 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- 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
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- 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
- B01J29/16—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J29/166—Y-type faujasite
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- 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
- B01J29/10—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing iron group metals, noble metals or copper
- B01J29/106—Y-type faujasite
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- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/633—Pore volume less than 0.5 ml/g
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- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
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- B01J35/66—Pore distribution
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- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/20—Faujasite type, e.g. type X or Y
- C01B39/24—Type Y
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- 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
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- 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
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- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
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- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/12—After treatment, characterised by the effect to be obtained to alter the outside of the crystallites, e.g. selectivation
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
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- B01J2229/37—Acid treatment
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Claims (24)
1. Катализатор гидрокрекинга, содержащий:
носитель;
аморфный кремнезем-глиноземистый материал;
стабилизированный цеолит Y, имеющий величину индексного показателя распределения кислотных центров от 0,02 до 0,12; и
по меньшей мере один металл, выбранный из группы, состоящей из элементов группы 6 и групп 8-10 Периодической таблицы элементов.
2. Катализатор по п. 1, отличающийся тем, что стабилизированный цеолит Y представляет собой стабилизированный цеолит Y с высоким объемом нанопор, имеющий объем нанопор в диапазоне размеров от 20 до 50 нм, от 0,15 до 0,6 куб.см/г.
3. Катализатор по п. 2, отличающийся тем, что от 20 до 30% нанопор имеют размеры в диапазоне от 8 до 20 нм.
4. Катализатор по п. 2, отличающийся тем, что от 40 до 60% нанопор имеют размеры в диапазоне от 20 до 50 нм.
5. Катализатор по п. 2, отличающийся тем, что от 15 до 25% нанопор имеют размеры более 50 нм.
6. Катализатор по п. 1, отличающийся тем, что стабилизированный цеолит Y с высоким объемом нанопор имеет величину индексного показателя распределения кислотных центров от 0,06 до 0,12.
7. Катализатор по п. 1, отличающийся тем, что стабилизированный цеолит Y с высоким объемом нанопор имеет величину индексного показателя распределения кислотных центров от 0,08 до 0,11.
8. Способ гидрокрекинга углеводородсодержащего сырья, включающий взаимодействие сырья с катализатором гидрокрекинга в условиях гидрокрекинга для получения выходящего продукта гидрокрекинга;
причем катализатор гидрокрекинга содержит:
носитель;
аморфный кремнезем-глиноземистый материал;
стабилизированный цеолит Y, имеющий величину индексного показателя распределения кислотных центров от 0,02 до 0,12; и
по меньшей мере один металл, выбранный из группы, состоящей из элементов группы 6 и групп 8-10 Периодической таблицы элементов.
9. Способ по п. 8, отличающийся тем, что стабилизированный цеолит Y представляет собой стабилизированный цеолит Y с высоким объемом нанопор, имеющий объем нанопор в диапазоне размеров от 20 до 50 нм, от 0,15 до 0,6 куб.см/г.
10. Способ по п. 9, отличающийся тем, что от 20 до 30% нанопор имеют размеры в диапазоне от 8 до 20 нм.
11. Способ по п. 9, отличающийся тем, что от 40 до 60% нанопор имеют размеры в диапазоне от 20 до 50 нм.
12. Способ по п. 9, отличающийся тем, что от 15 до 25% нанопор имеют размеры более 50 нм.
13. Способ по п. 8, отличающийся тем, что стабилизированный цеолит Y с высоким объемом нанопор имеет величину индексного показателя распределения кислотных центров от 0,06 до 0,12.
14. Способ по п. 8, отличающийся тем, что стабилизированный цеолит Y с высоким объемом нанопор имеет величину индексного показателя распределения кислотных центров от 0,08 до 0,11.
15. Способ по п. 8, отличающийся тем, что выходящий продукт гидрокрекинга представляет собой тяжелый средний дистиллятный продукт в диапазоне от 380 до 700°F (193-371°C).
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US14/529,794 US20160121313A1 (en) | 2014-10-31 | 2014-10-31 | Middle distillate hydrocracking catalyst containing highly a stabilized y zeolite with enhanced acid site distribution |
US14/529,794 | 2014-10-31 | ||
PCT/US2015/042355 WO2016069071A2 (en) | 2014-10-31 | 2015-07-28 | Middle distillate hydrocracking catalyst containing highly a stabilized y zeolite with enhanced acid site distribution |
Publications (2)
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RU2017118406A true RU2017118406A (ru) | 2018-12-04 |
RU2017118406A3 RU2017118406A3 (ru) | 2018-12-04 |
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RU2017118406A RU2017118406A (ru) | 2014-10-31 | 2015-07-28 | Катализатор гидрокрекинга средних дистиллятов, содержащий высокостабилизированный цеолит y с улучшенным распределением кислотных центров |
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Country | Link |
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US (1) | US20160121313A1 (ru) |
EP (1) | EP3212329A2 (ru) |
JP (3) | JP2018500151A (ru) |
KR (2) | KR20220165834A (ru) |
CN (2) | CN106999919A (ru) |
AU (1) | AU2015339950A1 (ru) |
CA (1) | CA2966402C (ru) |
RU (1) | RU2017118406A (ru) |
SG (2) | SG10202004621UA (ru) |
WO (1) | WO2016069071A2 (ru) |
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KR101895497B1 (ko) * | 2016-10-26 | 2018-10-04 | 에쓰대시오일 주식회사 | 경방향족 탄화수소 제조용 수소화 분해 반응 촉매, 이의 제조방법 및 이를 이용한 경방향족 탄화수소의 제조방법 |
CN113171802A (zh) * | 2020-11-30 | 2021-07-27 | 谷育英 | 一种丙烷脱氢制丙烯催化剂的活化还原方法 |
US11590485B2 (en) | 2021-01-13 | 2023-02-28 | Saudi Arabian Oil Company | Process for modifying a hydroprocessing catalyst |
FR3130640A1 (fr) | 2021-12-21 | 2023-06-23 | IFP Energies Nouvelles | Catalyseur comprenant un support à base de matrice silico-aluminique et de zéolithe, sa préparation et procédé d’hydrocraquage de charges hydrocarbonées |
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JP5547923B2 (ja) * | 2009-08-03 | 2014-07-16 | 出光興産株式会社 | 重質油水素化分解触媒及びそれを用いた重質油の水素化処理方法 |
US20110171121A1 (en) * | 2010-01-08 | 2011-07-14 | Rive Technology, Inc. | Compositions and methods for making stabilized mesoporous materials |
US20120275993A1 (en) * | 2011-04-28 | 2012-11-01 | Rive Technology, Inc. | Dehydroxylation pretreatment of inorganic materials in mesopore introduction process |
FR2994394B1 (fr) * | 2012-08-09 | 2015-08-21 | Eurecat Sa | Procede de passivation par un compose azote d'un catalyseur zeolitique, en particulier d'un catalyseur d'hydrocraquage |
WO2014098820A1 (en) * | 2012-12-19 | 2014-06-26 | Exxonmobil Research And Engineering Company | Mesoporous zeolite -y hydrocracking catalyst and associated hydrocracking processes |
US20150159095A1 (en) * | 2013-12-09 | 2015-06-11 | Bi-Zeng Zhan | Method for making a middle distillate |
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2014
- 2014-10-31 US US14/529,794 patent/US20160121313A1/en not_active Abandoned
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2015
- 2015-07-28 EP EP15750865.6A patent/EP3212329A2/en active Pending
- 2015-07-28 CN CN201580067783.8A patent/CN106999919A/zh active Pending
- 2015-07-28 RU RU2017118406A patent/RU2017118406A/ru not_active Application Discontinuation
- 2015-07-28 KR KR1020227042371A patent/KR20220165834A/ko active IP Right Grant
- 2015-07-28 AU AU2015339950A patent/AU2015339950A1/en not_active Abandoned
- 2015-07-28 WO PCT/US2015/042355 patent/WO2016069071A2/en active Application Filing
- 2015-07-28 JP JP2017523454A patent/JP2018500151A/ja active Pending
- 2015-07-28 SG SG10202004621UA patent/SG10202004621UA/en unknown
- 2015-07-28 CN CN202410149941.5A patent/CN117960231A/zh active Pending
- 2015-07-28 SG SG11201703503UA patent/SG11201703503UA/en unknown
- 2015-07-28 KR KR1020177013942A patent/KR20170078715A/ko not_active Application Discontinuation
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CA2966402A1 (en) | 2016-05-06 |
AU2015339950A8 (en) | 2017-05-25 |
KR20220165834A (ko) | 2022-12-15 |
SG10202004621UA (en) | 2020-06-29 |
CN117960231A (zh) | 2024-05-03 |
KR20170078715A (ko) | 2017-07-07 |
EP3212329A2 (en) | 2017-09-06 |
WO2016069071A2 (en) | 2016-05-06 |
JP2020182947A (ja) | 2020-11-12 |
US20160121313A1 (en) | 2016-05-05 |
CA2966402C (en) | 2023-09-19 |
AU2015339950A1 (en) | 2017-05-18 |
JP2018500151A (ja) | 2018-01-11 |
CN106999919A (zh) | 2017-08-01 |
JP2023093493A (ja) | 2023-07-04 |
RU2017118406A3 (ru) | 2018-12-04 |
SG11201703503UA (en) | 2017-05-30 |
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