The elementary irreversible gas phase reaction a → b + c is carried out in a pfr packed with catalyst. pure a enters the reactor at a volumetric flowrate of 20 dm3/s at a pressure of 10 atm and 450k part i- adiabatic operation a) plot the conversion and temperature down the plug flow reactor until 80% conversion is achieved. b) calculate the amount of catalyst required to achieve 80% conversion. ha--70 k/mol hrs -50 kj/mol hrc-40 kj/mol (tr 273 k) cpa-40 j/mol. k cp 25 j/mol. k cpc=15 /mol-k 0.133e sp r1450-ti kg cat s with e = 31.4 kl/mol part ii consider that the heat is removed by a heat exchanger jacketing the reactor. the flowrate of coolant through the jacket is sufficiently high so that the ambient exchanger temperature is constant at 50°c u 100 w/m2.k d-10 cm po-5 g/cm a) plot the conversion and temperature down the plug flow reactor until 80% conversion is achieved. discuss the effect of feed temperature on the temperature profile and conversion. b) calculate the amount of catalyst required to achieve 80% conversion.