초록 ▼

Methanol is prepared by catalytic conversion of a synthesis gas mixture, containing hydrogen, carbon monoxide, carbon dioxide and/or water, at from 200°to 320°C. and under from 30 to 300 bar in adiabatic and/or isothermal reactions in the presence of a catalyst containing copper and zinc, by a proce

Methanol is prepared by catalytic conversion of a synthesis gas mixture, containing hydrogen, carbon monoxide, carbon dioxide and/or water, at from 200°to 320°C. and under from 30 to 300 bar in adiabatic and/or isothermal reactions in the presence of a catalyst containing copper and zinc, by a process in which the fresh catalyst is reduced with a hydrogen-containing gas before the start-up of the process, and then the synthesis is started under conventional conditions and is continued until the formation of methanol in the reaction zone has declined substantially, after which the reaction is interrupted and the catalyst is regenerated.

대표청구항 ▼

A process for the preparation of methanol by catalytic conversion of a synthesis gas mixture, containing hydrogen, carbon monoxide, carbon dioxide and/or water, at from 200°to 320°C. and under from 30 to 300 bar in adiabatic and/or isothermal reactions in the presence of a catalyst containing copper

A process for the preparation of methanol by catalytic conversion of a synthesis gas mixture, containing hydrogen, carbon monoxide, carbon dioxide and/or water, at from 200°to 320°C. and under from 30 to 300 bar in adiabatic and/or isothermal reactions in the presence of a catalyst containing copper and zinc, wherein the fresh catalyst is first reduced with a hydrogen-containing gas before the start-up of the process, under atmospheric or slightly superatmospheric pressure at temperatures increasing from 150°to 250°C., the reduction being contained until the formation of water from the reduction reaction substantially declines, and then the synthesis is started under conventional conditions and is continued until the formation of methanol in the reaction zone has declined substantially, after which the reaction is interrupted and the catalyst is immediately flushed with an inert gas at from 10°to 300°C. and is regenerated in situ wherein the regeneration is carried out under atmospheric or moderately superatmospheric pressure, by passing an oxygen-containing gas over the catalyst at from 150°to 200°C., the oxygen content being adapted to the particular temperature during the entire course of the regeneration, and the passage of the oxygen-containing gas continuing until the peak of the temperature profile has moved across the entire catalyst.