SG11202005027XA - Modified y-type molecular sieve and preparation method thereof, hydrocracking catalyst and preparation method thereof, and method for hydrocracking hydrocarbon oil - Google Patents

Modified y-type molecular sieve and preparation method thereof, hydrocracking catalyst and preparation method thereof, and method for hydrocracking hydrocarbon oil

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Publication number
SG11202005027XA
SG11202005027XA SG11202005027XA SG11202005027XA SG11202005027XA SG 11202005027X A SG11202005027X A SG 11202005027XA SG 11202005027X A SG11202005027X A SG 11202005027XA SG 11202005027X A SG11202005027X A SG 11202005027XA SG 11202005027X A SG11202005027X A SG 11202005027XA
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Singapore
Prior art keywords
preparation
hydrocracking
modified
molecular sieve
hydrocarbon oil
Prior art date
Application number
SG11202005027XA
Inventor
Wei Liu
Minghua Guan
Yanze Du
Fenglai Wang
Bo Qin
Hang Gao
Original Assignee
China Petroleum & Chem Corp
Dalian Research Institute Of Petroleum And Petrochemicals Sinopec Corp
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Publication date
Application filed by China Petroleum & Chem Corp, Dalian Research Institute Of Petroleum And Petrochemicals Sinopec Corp filed Critical China Petroleum & Chem Corp
Publication of SG11202005027XA publication Critical patent/SG11202005027XA/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084Y-type faujasite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/10Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing iron group metals, noble metals or copper
    • B01J29/14Iron group metals or copper
    • B01J29/146Y-type faujasite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J29/00Catalysts comprising molecular sieves
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    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/16Crystalline 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
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/16Crystalline 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
    • B01J29/166Y-type faujasite
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/617500-1000 m2/g
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63Pore volume
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
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    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
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    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
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    • B01J37/08Heat treatment
    • B01J37/082Decomposition and pyrolysis
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    • B01J37/10Heat treatment in the presence of water, e.g. steam
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    • B01J37/30Ion-exchange
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline 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
    • C01B39/20Faujasite type, e.g. type X or Y
    • C01B39/24Type Y
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking 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
    • C10G47/12Inorganic carriers
    • C10G47/16Crystalline alumino-silicate carriers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking 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
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G67/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J2029/081Increasing the silica/alumina ratio; Desalumination
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/16After treatment, characterised by the effect to be obtained to increase the Si/Al ratio; Dealumination
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/18After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
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    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/18After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
    • B01J2229/186After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions
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    • B01J2229/32Reaction with silicon compounds, e.g. TEOS, siliconfluoride
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    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/70Catalyst aspects

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (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)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
SG11202005027XA 2017-11-29 2017-11-29 Modified y-type molecular sieve and preparation method thereof, hydrocracking catalyst and preparation method thereof, and method for hydrocracking hydrocarbon oil SG11202005027XA (en)

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PCT/CN2017/113629 WO2019104543A1 (en) 2017-11-29 2017-11-29 Modified y-type molecular sieve and preparation method therefor, hydrocracking catalyst and preparation method therefor, and method for hydrocracking hydrocarbon oil

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US (1) US11179705B2 (en)
EP (1) EP3718629A4 (en)
JP (1) JP7169354B2 (en)
KR (1) KR102428229B1 (en)
CA (1) CA3083830C (en)
RU (1) RU2744001C1 (en)
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CN112723370B (en) * 2019-10-28 2022-08-12 中国石油化工股份有限公司 High-acid-content modified Y-type molecular sieve and preparation method and application thereof
CN112717981B (en) * 2019-10-28 2022-04-08 中国石油化工股份有限公司 Hydrocracking catalyst, and preparation method and application thereof
CN112723372B (en) * 2019-10-28 2022-08-12 中国石油化工股份有限公司 Modified Y-type molecular sieve rich in medium-strong acid and preparation method and application thereof
CN110862096A (en) * 2019-11-19 2020-03-06 上海绿强新材料有限公司 High-silicon NaY molecular sieve and preparation method and application thereof
CN114433204B (en) * 2020-10-19 2023-09-01 中国石油化工股份有限公司 Hydrocracking catalyst and preparation method thereof
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CN114433184B (en) * 2020-10-19 2024-05-07 中国石油化工股份有限公司 Hydrocracking catalyst and preparation method and application thereof
CN114477215B (en) * 2020-10-23 2023-07-14 中国石油化工股份有限公司 Low-sodium content Y-type molecular sieve and preparation method thereof
CN114471687B (en) * 2020-10-26 2023-10-10 中国石油化工股份有限公司 Process for preparing bulk hydrocracking catalyst
CN114471742A (en) * 2020-10-27 2022-05-13 中国石油化工股份有限公司 Modified Y-type molecular sieve and preparation method and application thereof
CN114471675B (en) * 2020-10-27 2023-09-01 中国石油化工股份有限公司 Modified ZSM-5 molecular sieve for hydrodewaxing and preparation method thereof
CN114534773A (en) * 2020-11-24 2022-05-27 中国石油天然气股份有限公司 USY type molecular sieve modification method and application thereof
CN116060117B (en) * 2021-10-29 2024-04-05 中国石油化工股份有限公司 Catalytic diesel hydrocracking catalyst and preparation method thereof
CN116062766B (en) * 2021-10-29 2024-05-07 中国石油化工股份有限公司 Modified ZSM-5 molecular sieve and preparation method and application thereof
CN116060091A (en) * 2021-10-29 2023-05-05 中国石油化工股份有限公司 Modified Y-type molecular sieve and preparation method and application thereof
CN116062768B (en) * 2021-10-29 2024-05-03 中国石油化工股份有限公司 Modified ZSM-5 molecular sieve and preparation method and application thereof
CN114956956B (en) * 2022-05-07 2023-12-19 万华化学集团股份有限公司 Method for producing neopentyl glycol

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