Ube Industries, Inc.

Yasushi Yoshida

Ikuya Matsuura

Kuniaki Nitta

Adolfo Parmaliana

Shigeo Sasaki

Nicola Giordano

Francesco Frusteri

Osamu Takayasu

Disclosed is a process for controlling the degree of dispersion of a catalyst active component in the preparation of a metal/carrier solid catalyst, which comprises dry-blending an ultra-fine single crystal carrier material and an active component metal material, molding the blend, heating and maintaining the molded body in an inert gas at a temperature higher than and close to the melting point of the active component metal material, and heat-treating the molded body in the same atmosphere gas at a temperature higher than the decomposition temperature of the active component metal material.

Process for controlling degree of dispersion of active component of

A high-activity nickel type catalyst, which comprises a carrier compound of high-purity ultra-fine single-crystal magnesia having an average particle size of 100 to 2000 .ANG. or a BET specific surface area of 6 to 170 m.sup.2 /g and metallic nickel or nickel oxide uniformly and thoroughly dispersed on the surface of the carrier in a supported amount of 0.1 to 50% by weight as metallic nickel. The catalyst exhibits a high activity in the steam reforming of hydrocarbons, methanation of synthesis gases, and hydrogenation of cyclic and alicyclic unsaturated hydrocarbons.

High-activity nickel catalyst and process for preparation thereof

A process for preparing hydrocarbons having at least two carbon atoms by bringing a methane-containing gas maintained at a temperature of 500.degree. to 1500.degree. C. into contact with an oxygen-containing gas in the presence of a catalyst to effect oxidative coupling, using a catalyst comprising (1) a single-crystal, high-purity, and ultra-fine powdery magnesium oxide obtained by the gas-phase method, and (2) an alkali metal oxide.

Catalyst for preparation of hydrocarbons

A process for preparing hydrocarbons having at least two carbon atoms by bringing a methane-containing gas maintained at a temperature of 500 to 1500.degree. C. into contact with an oxygen-containing gas in the presence of a catalyst to effect oxidative coupling, using a catalyst comprising (1) a single-crystal, high-purity, and ultra-fine powdery magnesium oxide obtained by the gas-phase method, and (2) an alkali metal oxide.

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Ube, Japan

Yasushi Yoshida