GB1299387A - Hydro-denitrogenation-hydrocracking process - Google Patents

Hydro-denitrogenation-hydrocracking process

Info

Publication number
GB1299387A
GB1299387A GB1712870A GB1712870A GB1299387A GB 1299387 A GB1299387 A GB 1299387A GB 1712870 A GB1712870 A GB 1712870A GB 1712870 A GB1712870 A GB 1712870A GB 1299387 A GB1299387 A GB 1299387A
Authority
GB
United Kingdom
Prior art keywords
hydrocracking
hydrodenitrogenation
catalyst
oxide
aluminosilicate
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.)
Expired
Application number
GB1712870A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Standard Oil Co
Original Assignee
Standard Oil Co
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 filed Critical Standard Oil Co
Publication of GB1299387A publication Critical patent/GB1299387A/en
Expired legal-status Critical Current

Links

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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
    • 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
    • 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
    • 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

Abstract

1299387 Hydrodenitrogenation; hydrocracking STANDARD OIL CO 10 April 1970 [10 April 1969] 17128/70 Heading C5E A petroleum hydrocarbon feedstock boiling above 350‹ F. and containing 1-3000 p.p.m. nitrogen is treated with H 2 and a hydrodenitrogenation catalyst to give a denitrogenated effluent and the effluent is hydrocracked with a hydrocracking catalyst, the hydrodenitrogenation catalyst comprising a group VIa or VIII metal, oxide and/or sulphide hydrogenating component on a co-catalytic acidic support comprising large-pore crystalline aluminosilicate and a refractory metal oxide, and the hydrocracking catalyst comprising a group VIa or VIII metal, oxide and/or sulphide on an acidic support consisting of large-pore crystalline aluminosilicate. Prefered catalysts are denitrogenation: Ni and W in an ultra-stable aluminosilicate dispersed in a SiO 2 -Al 2 O 3 matrix; hydrocracking: Ni and W on an ultrastable aluminosilicate support. Preferably no separation is effected between the hydrodenitrogenation and the hydrocracking.
GB1712870A 1969-04-10 1970-04-10 Hydro-denitrogenation-hydrocracking process Expired GB1299387A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US81499769A 1969-04-10 1969-04-10

Publications (1)

Publication Number Publication Date
GB1299387A true GB1299387A (en) 1972-12-13

Family

ID=25216568

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1712870A Expired GB1299387A (en) 1969-04-10 1970-04-10 Hydro-denitrogenation-hydrocracking process

Country Status (7)

Country Link
JP (1) JPS507602B1 (en)
BE (1) BE748823A (en)
CA (1) CA938907A (en)
DE (1) DE2017287B2 (en)
FR (1) FR2038374B1 (en)
GB (1) GB1299387A (en)
NL (1) NL166494C (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE758640R (en) * 1970-01-02 1971-04-16 Standard Oil Co PROCESS FOR REFINING THE
ZA735587B (en) * 1972-08-21 1974-07-31 Universal Oil Prod Co Catalyst and method of manufacture
US4040979A (en) * 1976-02-23 1977-08-09 Uop Inc. Hydrocarbon conversion catalytic composite
FR2711667B1 (en) * 1993-10-25 1996-02-02 Inst Francais Du Petrole Process for the improved production of middle distillates together with the production of oils having high viscosity indices and viscosities, from heavy petroleum fractions.

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL296144A (en) * 1962-08-03
US3172836A (en) * 1962-12-28 1965-03-09 California Research Corp Hydrocarbon conversion process
DE1545307A1 (en) * 1965-12-28 1970-07-02 Gulf Research Development Co Process and catalyst for the hydrogenation cracking of hydrocarbons

Also Published As

Publication number Publication date
NL166494B (en) 1981-03-16
FR2038374A1 (en) 1971-01-08
BE748823A (en) 1970-09-16
CA938907A (en) 1973-12-25
FR2038374B1 (en) 1973-10-19
DE2017287B2 (en) 1981-06-04
JPS507602B1 (en) 1975-03-27
DE2017287A1 (en) 1970-10-15
NL166494C (en) 1981-08-17
NL7005091A (en) 1970-10-13

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee