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GB837821A - Composition of catalyst - Google Patents

Composition of catalyst

Info

Publication number
GB837821A
GB837821A GB1767/57A GB176757A GB837821A GB 837821 A GB837821 A GB 837821A GB 1767/57 A GB1767/57 A GB 1767/57A GB 176757 A GB176757 A GB 176757A GB 837821 A GB837821 A GB 837821A
Authority
GB
United Kingdom
Prior art keywords
alumina
silica
catalyst
cobalt
sulphide
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
GB1767/57A
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.)
Sinclair Refining Co
Original Assignee
Sinclair Refining 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 Sinclair Refining Co filed Critical Sinclair Refining Co
Publication of GB837821A publication Critical patent/GB837821A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/88Molybdenum
    • B01J23/882Molybdenum and cobalt

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

A catalyst comprises a support of silica and alumina, the alumina being in the range of 20 to 40% by weight of the silica and alumina, and at least one component consisting of iron, cobalt, nickel, molybdenum, tungsten, vanadium or tin, or an oxide or sulphide of such a metal. The support may contain magnesia in an amount not exceeding 10% by weight of the silica, alumina and magnesia. Mixtures of compounds may be used, such as nickel molybdate, tungstate, thiomolybdate or thiotungstate; mixtures of nickel oxides with molybdenum or tungsten oxide; cobalt-molybdena, cobalt thiomolybdena; and tungsten sulphide and nickeltungsten sulphide. The silica-alumina support may be treated with a cationic, anionic or non-ionic surface-active agent. The catalyst is used for the hydrocracking of residual petroleum fractions at 700 DEG to 1000 DEG F., at a pressure of 500 to 3000 p.s.i.g., and treating 0.5 to 5 pounds of oil per pound of catalyst per hour. In an example aluminium sulphate solution is added to a solution of sodium silicate and sulphuric acid to obtain a silica-alumina gel, which is impregnated with a solution of ammonium molybdate and cobalt nitrate, dried, pelleted and calcined. The catalyst is heated in a stream of hydrogen, and then in hydrogen sulphide to convert the cobalt and molybdenum oxides to sulphides, followed by hydrogen again, and a virgin gas oil is cracked by passing it over the heated catalyst. Specification 816,307 is referred to.
GB1767/57A 1956-01-17 1957-01-17 Composition of catalyst Expired GB837821A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US837821XA 1956-01-17 1956-01-17

Publications (1)

Publication Number Publication Date
GB837821A true GB837821A (en) 1960-06-15

Family

ID=22180662

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1767/57A Expired GB837821A (en) 1956-01-17 1957-01-17 Composition of catalyst

Country Status (1)

Country Link
GB (1) GB837821A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1795535B1 (en) * 1966-07-28 1972-05-31 Chevron Res Process for the hydrogenation conversion of hydrocarbons
CN116173980A (en) * 2023-03-08 2023-05-30 南京工业大学 A 3D printing reforming hydrogen production catalyst using waste vanadium-titanium denitrification catalyst as raw material and its preparation method and application

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1795535B1 (en) * 1966-07-28 1972-05-31 Chevron Res Process for the hydrogenation conversion of hydrocarbons
CN116173980A (en) * 2023-03-08 2023-05-30 南京工业大学 A 3D printing reforming hydrogen production catalyst using waste vanadium-titanium denitrification catalyst as raw material and its preparation method and application

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