METHOD FOR STARTING HYDROGENATION REACTOR OF OLEFIN PRODUCTION PLANT

摘要

start the reactor u0433u0438u0434u0440u0438u0440u043eu0432u0430u043du0438u00a0 installation u043fu043eu043bu0443u0447u0435u043du0438u00a0 olefins u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442, u0440u0430u0437u043eu0433u0440u0435u0432u0430u00a0 reactor temperatures u0433u0438u0434u0440u0438u0440u043eu0432u0430 - u043du0438u00a0 in the pipes of which is available. and in u043cu0435u0436u0442u0440u0443u0431u043du043eu043c space circulates refrigerant through the heating further u043fu043eu0434u043eu0433u0440u0435u0432u0430u0442u0435u043bu0435 u0446u0438u0440u043au0443u043bu0438u0440u0443u044eu0449u0435u0433u043e refrigerant, and then the heated reactor serves the heated raw material is in u043fu043eu0434u043eu0433u0440u0435u0432u0430u0442u0435u043bu0435 u043eu043bu0435u0444u0438u043du043eu0432u0443u044e fraction and hydrogen. 1 il.