Low-temperature, high-pressure, catalytic, partial conversion of naphtha hydrocarbons to hydrogen
In a process for steam-reforming liquid and/or gaseous hydrocarbons over a nickel catalyst at 550 DEG to 900 DEG F. (288 DEG to 482 DEG C.) at a pressure of 150 to 1500 p.s.i.g., the surface area of the nickel is initially 20 to 60 m.2 per gram, and the space velocity is controlled so that the hydro...
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