FIELD: hydrocarbon- containing waste disposal. SUBSTANCE: nickel-containing catalyst and inert material (carbon or aluminum oxide) at weight ratio 1 to at least 15 are placed into fluidized-bed reactor. Mixture is converted into fluidized or vibro-fluidized state and heated to 450-650 C. Through gas-distribution grille, hydrocarbon-containing gas is supplied. Yield of carbon attains 155 g/g, and that of hydrogen ranges from 26 to 38.8 l/h, while catalyst agglomeration is not detected. EFFECT: enhanced process efficiency. 3 cl, 2 dwg
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Authors
Dates
1998-04-10—Published
1995-02-28—Filed