CATALYST FOR HYDROFINING AGAINST ACETYLENE ETHANE-ETHYLENE FRACTION OF HYDROCARBON RAW MATERIALS PYROLYSIS

摘要

the invention u043eu0442u043du043eu0441u0438u0442u0441u00a0 to catalytic chemistry, in particular to u043au0430u0442u0430u043bu0438u0437u0430u0442u043eu0440u0443 u0434u043bu00a0 hydro ethane - u044du0442u0438u043bu0435u043du043eu0432u043eu0439 faction gas pyrolysis hydrocarbon u0441u044bu0440u044cu00a0 from u0430u0446u0435u0442u0438 lena to the chain u043fu043eu0432u044bu0448u0435u043du0438u00a0 selectivity and u0442u0435u0440u043cu043eu0441u0442u0430u0431u0438u043bu044cu043du043eu0441u0442u0438 with oxidizing catalyst regeneration is the ratio of the components of it.per cent palladium 0.05 - 0.3; u0430u043bu044eu043cu0438u043du0438u00a0 oxide containing 0.05 - 0.3; host - the u0434u043bu00a0 u0430u043bu044eu043cu0438u043du0438u00a0 oxide catalyst using metal palladium, distributed in captivity ke u0430u043bu044eu043cu0438u043du0438u00a0 oxide mass u0441u043eu043eu0442u043du043eu0448u0435u043du0438u00a0 u043fu0430u043bu043bu0430u0434u0438u00a0u043c oxide u0430u043bu044eu043cu0438u043du0438u00a0 1: 1. table 3