DE2064521A1 - Katalysator, der ultrastabile Aluminosilicate umfasst, und Kohlenwas serstoffumwandlungsverfahren, die diese Katalysatoren verwenden - Google Patents

Katalysator, der ultrastabile Aluminosilicate umfasst, und Kohlenwas serstoffumwandlungsverfahren, die diese Katalysatoren verwenden

Info

Publication number
DE2064521A1
DE2064521A1 DE19702064521 DE2064521A DE2064521A1 DE 2064521 A1 DE2064521 A1 DE 2064521A1 DE 19702064521 DE19702064521 DE 19702064521 DE 2064521 A DE2064521 A DE 2064521A DE 2064521 A1 DE2064521 A1 DE 2064521A1
Authority
DE
Germany
Prior art keywords
catalyst
ultra
stable
aluminosilicate
hydrocracking
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
DE19702064521
Other languages
German (de)
English (en)
Inventor
Albert Lloyd Munster Ind Hensleyjun (V St A )
Original Assignee
Standard Oil Co , Chicago, 111 (V St A )
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 Standard Oil Co , Chicago, 111 (V St A ) filed Critical Standard Oil Co , Chicago, 111 (V St A )
Publication of DE2064521A1 publication Critical patent/DE2064521A1/de
Ceased legal-status Critical Current

Links

Classifications

    • 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
    • B01J29/16—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
    • 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
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/16—Alumino-silicates
    • B01J20/18—Synthetic zeolitic molecular sieves
    • B01J20/186—Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity
    • 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
    • B01J29/16—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
    • 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
    • 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
    • C10G61/00—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen
    • C10G61/02—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only
    • C10G61/06—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only the refining step being a sorption process
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
DE19702064521 1970-01-02 1970-12-30 Katalysator, der ultrastabile Aluminosilicate umfasst, und Kohlenwas serstoffumwandlungsverfahren, die diese Katalysatoren verwenden Ceased DE2064521A1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US20470A 1970-01-02 1970-01-02
US18400571A 1971-09-27 1971-09-27
US394041A US3894930A (en) 1970-01-02 1973-09-04 Catalyst comprising ultrastable aluminosilicates and hydrocarbon conversion processes employing same

Publications (1)

Publication Number Publication Date
DE2064521A1 true DE2064521A1 (de) 1971-07-08

Family

ID=27356623

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19702064521 Ceased DE2064521A1 (de) 1970-01-02 1970-12-30 Katalysator, der ultrastabile Aluminosilicate umfasst, und Kohlenwas serstoffumwandlungsverfahren, die diese Katalysatoren verwenden

Country Status (4)

Country Link
US (1) US3894930A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
BE (1) BE758640R (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
DE (1) DE2064521A1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
FR (1) FR2075895B2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4981576A (en) * 1979-03-19 1991-01-01 Amoco Corporation Process for the hydrodenitrogenation and hydrocracking of high nitrogen feeds
US4460698A (en) * 1981-11-13 1984-07-17 Standard Oil Company (Indiana) Hydrocarbon conversion catalyst
USRE33728E (en) * 1981-11-24 1991-10-29 Total Engineering And Research Company Method for catalytically converting residual oils
US4962269A (en) * 1982-05-18 1990-10-09 Mobil Oil Corporation Isomerization process
US4820402A (en) * 1982-05-18 1989-04-11 Mobil Oil Corporation Hydrocracking process with improved distillate selectivity with high silica large pore zeolites
CA1264880A (en) * 1984-07-06 1990-01-23 John Brooke Gardiner Viscosity index improver - dispersant additive useful in oil compositions
US5013422A (en) * 1986-07-29 1991-05-07 Mobil Oil Corp. Catalytic hydrocracking process
US5041208A (en) * 1986-12-04 1991-08-20 Mobil Oil Corporation Process for increasing octane and reducing sulfur content of olefinic gasolines
US5817903A (en) * 1997-04-04 1998-10-06 Phillips Petroleum Company Hydrotreating catalyst composition and processes therefor and therewith
CN115974095B (zh) * 2022-12-07 2024-05-31 广东能源集团科学技术研究院有限公司 一种中空多级孔复合分子筛及其制备方法和应用

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1386663A (fr) * 1964-02-04 1965-01-22 Socony Mobil Oil Co Procédé perfectionné de craquage hydrogénant catalytique
US3222416A (en) * 1961-12-18 1965-12-07 Shell Oil Co Extraction process
US3293192A (en) * 1965-08-23 1966-12-20 Grace W R & Co Zeolite z-14us and method of preparation thereof
GB1058188A (en) * 1963-02-27 1967-02-08 Mobil Oil Corp Method for preparing highly siliceous zeolite-type materials and materials resulting therefrom
FR1482865A (fr) * 1965-01-21 1967-06-02 Mobil Oil Corp Hydrocraquage catalytique
DE1253389B (de) * 1962-09-11 1967-11-02 Exxon Research Engineering Co Verfahren zum gegebenenfalls hydrierenden Spalten von Kohlenwasserstoffen
DE2000026B2 (de) * 1969-01-03 1979-12-06 Standard Oil Co., Chicago, Ill. (V.St.A.) Verfahren zur Umwandlung eines Petroleumkohlenwasserstoff-Beschickungsmaterials in ein niedriger siedendes . Produkt

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3008895A (en) * 1959-08-25 1961-11-14 Union Oil Co Production of high-octane gasolines
US3431196A (en) * 1967-02-21 1969-03-04 Dobres Amalie B Hydrocracking catalyst and process
US3649523A (en) * 1969-04-10 1972-03-14 Standard Oil Co Hydrocracking process and catalyst
NL166494C (nl) * 1969-04-10 1981-08-17 Standard Oil Co Werkwijze voor het hydrokraken van een mengsel van petroleumkoolwaterstoffen, dat boven 180 graden c kookt en 1 tot 3000 mg/kg stikstof bevat.
US3617509A (en) * 1969-07-07 1971-11-02 Standard Oil Co Catalytic composition, method of preparing same, and hydrocarbon-conversion process employing same
US3597349A (en) * 1969-10-29 1971-08-03 Standard Oil Co Catalytic composition comprising a particulate mixture of ultrastable aluminosilicate - containing silica-alumina and cation-exchanged y-type molecular sieves and processes employing same

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3222416A (en) * 1961-12-18 1965-12-07 Shell Oil Co Extraction process
DE1253389B (de) * 1962-09-11 1967-11-02 Exxon Research Engineering Co Verfahren zum gegebenenfalls hydrierenden Spalten von Kohlenwasserstoffen
GB1058188A (en) * 1963-02-27 1967-02-08 Mobil Oil Corp Method for preparing highly siliceous zeolite-type materials and materials resulting therefrom
FR1386663A (fr) * 1964-02-04 1965-01-22 Socony Mobil Oil Co Procédé perfectionné de craquage hydrogénant catalytique
FR1482865A (fr) * 1965-01-21 1967-06-02 Mobil Oil Corp Hydrocraquage catalytique
US3293192A (en) * 1965-08-23 1966-12-20 Grace W R & Co Zeolite z-14us and method of preparation thereof
DE2000026B2 (de) * 1969-01-03 1979-12-06 Standard Oil Co., Chicago, Ill. (V.St.A.) Verfahren zur Umwandlung eines Petroleumkohlenwasserstoff-Beschickungsmaterials in ein niedriger siedendes . Produkt

Also Published As

Publication number Publication date
FR2075895B2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) 1974-03-22
US3894930A (en) 1975-07-15
BE758640R (fr) 1971-04-16
FR2075895A2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) 1971-10-15

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