Acetylene removal process

Claim 1

In a vapor phase process for the preparation of hydrocarbon monoolefins and diolefins comprising oxidative dehydrogenation of a stream of C 3 to C 9 hydrocarbon compounds to produce a product stream comprising, exclusive of any water present, 3.5 to 80 mol percent hydrocarbon monoolefins and diolefins and about from 0.0001 to 2.5 mol percent acetylenic compound impurity, about from 0.0005 to 2.5 mol percent carbonyl compounds and 5 to 93 mol percent non-condensable gases, wherein the improvement comprises contacting said product stream in vapor phase at a temperature in the range of 250° to 900° C. and containing less than 5 mol percent free oxygen with a solid catalyst for reducing said acetylene compounds in said product stream, said catalyst consisting essentially of zinc ferrite and nickel oxide, wherein Fe is the major metal component by weight, an alkaline earth metal oxide, carbonate or hydroxide of Mg, Ca, Sr or Ba, and about 0.5 to 30 weight percent of an alkali metal oxide, carbonate or hydroxide, based on the other metallic elements of Li, Na, K or Rb said Ni being present in the range of 0.25 to 20 weight percent of the total weight of the catalyst, and recovering said product stream having the amount of acetylenic compounds therein reduced.