A 400-L CSTR and a 100-L PFR are available to process 1.0L of feed per second. The feed contains 41% A, 41% B, and 18% inests. The irreversible gas-phase reaction A+BC is to be carried out at 10 atm and 227C. The rate of reaction in g mol/L. min is given below as a function of conversion: * 0.2 0.0167 0.00488 0.00286 0.00204 X 0.0 0.1 04 0.7 0.9 (a) What is the maximum conversion that can be achieved with these two reactors connected in series? (6) What would be the overall conversion if two 400-L CSTRs were connected in series for the same feed and operating conditions? (e) What would be the overall conversion if two 400-L CSTRs were connected in parallel with half of the feed going to each reactor? (a) What is the volume of a single tubular reactor necessary to achieve 60% conversion if the molar feed rate is 2 g mol A/min? (e) If the total pressure were reduced by a factor of 10, would the conversion increase, decrease, or remain the same? (1) Plot the rate of reaction and conversion as a function of PFR volume