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Consider the following data for ethylene hydrogenation to ethane in a batch reactor:
C2H4 + H2 → C2H6
The reaction may be considered to be first-order and irreversible:
Data
T = 100 °C
Initial PC2H4 = 350 torr
Initial PH2 = 612 torr
Mass of catalyst = 0.43 g
Volume of catalyst = 0.21 cm3
Catalyst: 0.3 x 0.3 cm cylinders
Pore radius = 100 Å
Assuming that only Knudsen diffusion is present, evaluate these data to determine if pore diffusion mass transport may be limiting.
what is the name of the theory that explains plate movement?
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