Hydrogen production

Details Hydrogen production Hydrogen production

C - Chemistry, Metallurgy

01

B

23/316

C01B 3/02 (2006.01) C01B 3/16 (2006.01)

Patent

CA 1249420

Abstract Hydrogen production Catalytic shift is effected in a reactor provided using a copper catalyst in indirect heat exchange with boiling water at a gas flow rate of 200 to 800 kg mol per hour per m3 of catalyst. The shift is effected using an outlet temperature in the range 230 to 280°C that is preferably 10 to 30°C below the maximum, or inlet, temperature. The heat exchange surface is 30 to 200 m2 per m3 of catalyst.

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