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Simultaneous shift reaction and carbon dioxide separation for the direct production of hydrogen

✍ Scribed by Chun Han; Douglas P. Harrison


Publisher
Elsevier Science
Year
1994
Tongue
English
Weight
769 KB
Volume
49
Category
Article
ISSN
0009-2509

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Investigation of simultaneous reaction o
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The kinetics of low-pressure methanol synthesis from CO, CO, and H, on a commercial Cu/ZnO catalyst was investigated in a Berty-type reactor at low overall conversion to reduce the influence of chemical equilibria (reaction conditions: p = 3-5 MPa, T = 483-543 K). At constant Hz partial pressure the