GB939213A - Method of making a nickel-magnesium hydrocarbon-steam reforming catalyst - Google Patents

Method of making a nickel-magnesium hydrocarbon-steam reforming catalyst

Info

Publication number
GB939213A
GB939213A GB196460A GB196460A GB939213A GB 939213 A GB939213 A GB 939213A GB 196460 A GB196460 A GB 196460A GB 196460 A GB196460 A GB 196460A GB 939213 A GB939213 A GB 939213A
Authority
GB
United Kingdom
Prior art keywords
steam reforming
nickel
calcining
binder
grinding
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
GB196460A
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.)
Chemetron Corp
Original Assignee
Chemetron Corp
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 Chemetron Corp filed Critical Chemetron Corp
Publication of GB939213A publication Critical patent/GB939213A/en
Expired 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

Hydrogen and carbon oxides are formed by effecting the hydrocarbon-steam reforming reaction in presence of a catalyst prepared by admixing a nickel compound (the oxide or a compound convertible thereto by heating in air) with alumina or magnesia and with a binder, and sufficient water to provide a dough-like mass, shaping, calcining the shapes to incipient fusion and grinding the calcined product. A ball clay, kaolin or bentonite may be used as an additional component of the catalyst mixture. The binder has the composition CaO 60-67%, SiO2 18,5-25,5%, Al2O3 3-7,5%, MgO 0,5-5,5%, other metal oxides (impurities, e.g. Fe2O3, alkali and alkaline earth metal oxides excluding CaO) balance; it is prepared by calcining to incipient fusion a mixture of calcaveous and argillaceous materials and grinding the product. Examples are given.
GB196460A 1959-01-26 1960-01-19 Method of making a nickel-magnesium hydrocarbon-steam reforming catalyst Expired GB939213A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US78871659A 1959-01-26 1959-01-26

Publications (1)

Publication Number Publication Date
GB939213A true GB939213A (en) 1963-10-09

Family

ID=25145334

Family Applications (1)

Application Number Title Priority Date Filing Date
GB196460A Expired GB939213A (en) 1959-01-26 1960-01-19 Method of making a nickel-magnesium hydrocarbon-steam reforming catalyst

Country Status (1)

Country Link
GB (1) GB939213A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1272897B (en) * 1963-10-19 1968-07-18 Azote Office Nat Ind Process for the production of nickel carrier catalysts with carriers containing magnesium oxide
US3408171A (en) * 1964-10-05 1968-10-29 Azote Office Nat Ind Process of steam reforming paraffinic hydrocarbons
DE1282834B (en) * 1965-05-28 1968-11-14 Koppers Gmbh Heinrich Process for generating hydrogen-containing gases, the methane content of which can be set in the range between less than 1 and 55 percent by volume, by catalytic conversion of gasoline hydrocarbons containing less than 1 ppm of sulfur with water vapor under increased pressure

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1272897B (en) * 1963-10-19 1968-07-18 Azote Office Nat Ind Process for the production of nickel carrier catalysts with carriers containing magnesium oxide
US3408171A (en) * 1964-10-05 1968-10-29 Azote Office Nat Ind Process of steam reforming paraffinic hydrocarbons
DE1282834B (en) * 1965-05-28 1968-11-14 Koppers Gmbh Heinrich Process for generating hydrogen-containing gases, the methane content of which can be set in the range between less than 1 and 55 percent by volume, by catalytic conversion of gasoline hydrocarbons containing less than 1 ppm of sulfur with water vapor under increased pressure

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