Abstract: A catalyst for oxidative coupling of methane comprising Fe.sub.2 O.sub.3 deposited on a silica substrate, said silica substrate having particle sizes in the range of about 150 to 215 .mu.m, and a method for producing said catalyst in which particles of Fe.sub.2 O.sub.3, with a particle size in the range from 100 to 150 .mu.m, and particles of silica, with a particle size in the range from about 150 to about 215 .mu.m are mixed together. The particles are heated to a temperature of at least about 800.degree. C., after which the silica particles impregnated with Fe.sub.2 O.sub.3 are separated from the remaining iron particles.

Abstract: A method of producing an oxidative coupling catalyst is disclosed by mixing particles of Fe.sub.2 O.sub.3, with a particle size in the range from 100 to 150 .mu.m, and silica, with a particle size in the range from about 150 to about 215 .mu.m. The particles are heated to a temperature of at least about 800.degree. C., after which the silica particles impregnated with Fe.sub.2 O.sub.3 are separated from the remaining iron particles. The catalyst can be utilized for the oxidative coupling of methane with water molecules on the surface of the silica substrate, with the silica having a particle size in the range from about 150 to about 215.ltoreq..mu.m. The silicate catalyst substrate is essentially non-porous and has an average geometrical surface on the order of about 0.004 .mu.m.sup.2 /g and a surface concentration of iron on the order of about 2% by weight.