Description
Dry reforming of methane and carbon dioxide to produce synthetic gas can be written as
follows
With the production rate of 100000 tonnes per year using a fixed bed reactor and at 900
°𝐶, it is found that the weight of catalyst required is approximately 34200𝑘𝑔. If steel tube
of diameter 0.0762𝑚 (3 inches) is recommended, propose a set of acceptable conditions
under which, the external concentration difference between the bulk concentration and
catalyst pellet external surface concentration of a reactant (CO2) is less than 0.00036
𝑚𝑜𝑙𝑚3. State all the assumptions made.
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