A packed bed reactor has the reaction A --> B occurring. The rate law is –rA = kCA where k = 15 L/g-min. The superficial gas velocity is 4.8 kg/m2-s with a density of 0.45 kg/m3 and a viscosity of 3.9x10-5 kg/m-s. The porosity, catalyst density, and particle diameter are, respectively, 0.45, 2.2 g/cm3 and 0.255 cm. The cross sectional area of the reactor is 12 cm2. The inlet pressure is 100 kPa. Calculate the conversion ‘X’ when the catalyst mass in the PBR is 130 g.
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