IE31986L - Catalytic hydrocracking proces - Google Patents

Catalytic hydrocracking proces

Info

Publication number
IE31986L
IE31986L IE31468A IE31468A IE31986L IE 31986 L IE31986 L IE 31986L IE 31468 A IE31468 A IE 31468A IE 31468 A IE31468 A IE 31468A IE 31986 L IE31986 L IE 31986L
Authority
IE
Ireland
Prior art keywords
catalyst
tungsten
nickel
proces
catalytic hydrocracking
Prior art date
Application number
IE31468A
Other versions
IE31986B1 (en
Original Assignee
Exxon Research Engineering 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
Priority claimed from US627806A external-priority patent/US3394074A/en
Application filed by Exxon Research Engineering Co filed Critical Exxon Research Engineering Co
Publication of IE31986L publication Critical patent/IE31986L/en
Publication of IE31986B1 publication Critical patent/IE31986B1/en

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
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (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)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

1,219,328. Zeolites. ESSO RESEARCH & ENG. CO. 18 March, 1968 [3 April, 1967; 24 May, 1967], No. 12917/68. Heading C1A. [Also in Divisions B1 and C5] A catalyst for hydrocracking petroleum products consists of the hydrogen or hydrogenprecursor form of a crystalline aluminosilicate zeolite having uniform pore diameters, the crystal structure of a faujasite and a silica to alumina mol. ratio exceeding 3 plus 1 to 8% by weight of nickel and 3 to 18% of tungsten (calculated as metal) which may be sulphided. The nickel may be introduced by base exchange or by impregnation, the catalyst then being treated with ammonium tungstate to introduce the tungsten. The catalyst may be baseexchanged with rare earths. [GB1219328A]
IE31468A 1967-04-03 1968-03-19 Improved hydrocracking process utilizing mixed nonnoble metal catalyst IE31986B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US627806A US3394074A (en) 1967-04-03 1967-04-03 Single reactor hydrocracking process with mixed nonnoble metal catalyst for full boiling raw feed
US64085967A 1967-05-24 1967-05-24

Publications (2)

Publication Number Publication Date
IE31986L true IE31986L (en) 1968-10-03
IE31986B1 IE31986B1 (en) 1973-03-07

Family

ID=27090535

Family Applications (1)

Application Number Title Priority Date Filing Date
IE31468A IE31986B1 (en) 1967-04-03 1968-03-19 Improved hydrocracking process utilizing mixed nonnoble metal catalyst

Country Status (9)

Country Link
JP (1) JPS5016362B1 (en)
BE (1) BE713107A (en)
DE (1) DE1770125B2 (en)
FR (1) FR1560101A (en)
GB (1) GB1219328A (en)
IE (1) IE31986B1 (en)
NL (1) NL6804596A (en)
NO (1) NO125101B (en)
SE (1) SE345871B (en)

Also Published As

Publication number Publication date
NO125101B (en) 1972-07-17
SE345871B (en) 1972-06-12
IE31986B1 (en) 1973-03-07
GB1219328A (en) 1971-01-13
DE1770125B2 (en) 1973-01-11
DE1770125A1 (en) 1972-04-13
FR1560101A (en) 1969-03-14
JPS5016362B1 (en) 1975-06-12
NL6804596A (en) 1968-10-04
BE713107A (en) 1968-10-02

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