Methanol production over a copper-zinc oxide catalyst has been extensively investigated recently. Data indicated a strong dependence of the kinetics on the gas composition. The kinetics can be determined at well-controlled gas compositions, achieved either by using a differential flow reactor, or by using a batch reactor and performing initial rate measurements. This paper describes results of the latter approach.
|Title of host publication||Annual Meeting - American Institute of Chemical Engineers|
|Publication status||Published - 1984|
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