发明名称 |
PRODUCING HYDROGEN BY CATALYTIC SHIFT REACTION |
摘要 |
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 m<3> of catalyst. The shift is effected using an outlet temperature in the range 230 to 280 DEG C that is preferably 10 to 30 DEG C below the maximum, or inlet, temperature. The heat exchange surface is 30 to 200 m<2> per m<3> of catalyst. |
申请公布号 |
AU6172986(A) |
申请公布日期 |
1987.03.05 |
申请号 |
AU19860061729 |
申请日期 |
1986.08.21 |
申请人 |
IMPERIAL CHEMICAL INDUSTRIES PLC |
发明人 |
ALWYN PINTO;IAN CHARLES JEFFERY |
分类号 |
C01B3/14;C01B3/16;C01B3/48 |
主分类号 |
C01B3/14 |
代理机构 |
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代理人 |
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主权项 |
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地址 |
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