Question
Partial oxidation of methane with excess of oxygen takes place at 1 atm and 200°C in a continuous tubular reactor, according to R1: C H_{4}(g)+\frac{3}{2} O_{2}(g) \rightarrow C O(g)+2 H_{2} O(g) The reactor is designed to reach a 50% fractional conversion of a vChala)in= 200 L min-1 methane inlet, xCHa(g)= 0.5. Assum
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