GB946026A - Process for imparting increased activity to inorganic solid contact material - Google Patents

Process for imparting increased activity to inorganic solid contact material

Info

Publication number
GB946026A
GB946026A GB1021461A GB1021461A GB946026A GB 946026 A GB946026 A GB 946026A GB 1021461 A GB1021461 A GB 1021461A GB 1021461 A GB1021461 A GB 1021461A GB 946026 A GB946026 A GB 946026A
Authority
GB
United Kingdom
Prior art keywords
inorganic oxide
alumina
sulphur trioxide
temperature
reducing atmosphere
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
GB1021461A
Inventor
William Galloway Nixon
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products 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 Universal Oil Products Co filed Critical Universal Oil Products Co
Priority to GB1021461A priority Critical patent/GB946026A/en
Publication of GB946026A publication Critical patent/GB946026A/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
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/20Sulfiding
    • 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
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • 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
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/42Platinum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0207Pretreatment of the support

Landscapes

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

Abstract

Increased activity is imparted to an adsorptive refractory inorganic oxide by contacting the inorganic oxide, while in a hydrous state, at a temperature in excess of 100 DEG C. with sulphur trioxide in a non-reducing atmosphere. The refractive inorganic oxide can be alumina, silica, magnesia, thoria, zirconia, titania, boria or mixtures of two or more of these oxides; they may be naturally occurring earth, clays, sands and/or minerals, or they may be synthetically prepared. The invention is particularly applicable to alumina, silica and mixtures of the two. In a specific embodiment an adsorptive refractory inorganic oxide material which has not been heated to any temperature above 150 DEG C., is contacted with sulphur trioxide between 100 DEG and 500 DEG C. in a non-reducing atmosphere and the oxide is then calcined at a temperature of at least 500 DEG C. To ensure the non-reducing atmosphere the adsorptive refractory inorganic oxide may be purged, prior to the sulphur trioxide treatment, with any suitable gaseous material which reacts neither with the refractory oxide nor with the sulphur trioxide, e.g. air, nitrogen, argon and other inert gases may be used. In the example, wet calcined alumina spheres prepared by the oil drop method are washed with methyl alcohol and water to remove any contaminants and allowed to dry in air at room temperature. A portion of the dried spheres are treated with a sulphur trioxide gas mixture formed by the oxidation of sulphur dioxide with air over a platinum catalyst, the temperature being gradually increased from 150 to 500 DEG C. The treated alumina had a surface area of 325 sq. metres/gm.-a 62% increase over untreated alumina.ALSO:A solid contact material consisting at least predominantly of an adsorptive refractory inorganic oxide which has been activated by contacting the inorganic oxide component while in a hydrous state, at a temperature greater than 100 DEG C. with sulphur trioxide in a non-reducing atmosphere (see Division C1), is used as a carrier for a catalytically active metal component. The adsorptive refractory inorganic oxide is first activated as above and then impregnated with a minor proportion of a catalytically active metal component; metal components mentioned are platinum, iridium, palladium, ruthenium, rhodium, osmium, iron, cobalt, nickel, chromium, molybdenum, and tungsten. The amount of metal component used is generally such that the final catalyst composite contains 0,01-20% by weight of the metal component. The carrier material which may for example be alumina, silica, magnesia, thoria, zirconia, titania, boria or mixtures thereof, or a naturally occuring earth, clay, sand, and/or minerals (or a synthetically prepared material), may be impregnated with a halogen and used in the reforming of hydrocarbons.
GB1021461A 1961-03-21 1961-03-21 Process for imparting increased activity to inorganic solid contact material Expired GB946026A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1021461A GB946026A (en) 1961-03-21 1961-03-21 Process for imparting increased activity to inorganic solid contact material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1021461A GB946026A (en) 1961-03-21 1961-03-21 Process for imparting increased activity to inorganic solid contact material

Publications (1)

Publication Number Publication Date
GB946026A true GB946026A (en) 1964-01-08

Family

ID=9963694

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1021461A Expired GB946026A (en) 1961-03-21 1961-03-21 Process for imparting increased activity to inorganic solid contact material

Country Status (1)

Country Link
GB (1) GB946026A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4894357A (en) * 1984-11-02 1990-01-16 Kali-Chemie Aktiengesellschaft Process for adjusting the structural and/or surface character of oxides

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4894357A (en) * 1984-11-02 1990-01-16 Kali-Chemie Aktiengesellschaft Process for adjusting the structural and/or surface character of oxides

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