All the other answers on chegg were wrong or incomplete. Please don't copy them

ABwithk=4.54107cm3mol1s1 Pure A is fed to the reactor and a conversion of 93% is achieved at a pressure of 2.0atm. The total volumetric feed rate into the reactor is 1000Lsec1. The catalyst vendor has changed fabrication procedures and has verified that the intrinsic (kinetic) rate constant listed above is unchanged. Note that the volumetric rate calculated with the above rate constant is the rate per volume of catalyst bed. The following data is available: For this problem, you may assume that the surface concentration is always equal to the concentration of species in the bulk fluid (i.e., external diffusion is very fast), that diffusion in either particle only occurs in the radial dimension, and that there is no pressure drop in the reactor. Part 1 Determine the mass of the old catalyst formulation used in the reactor. Part 2 Determine If the mass of catalyst needs to be changed for the new catalyst to maintain the same conversion of A and production of B Part 3 If the catalyst mass needs to be changed, what is the mass of new catalyst required