The acid-catalyzed irreversible liquid-phase reaction AB is carried out adiabatically in a CSTR. The reaction is second order in A. The feed, which is equimolar in a solvent (which contains the catalyst) and A, enters the reactor at a total volumetric flow rate of 10 dm3/min with the concentration of A being 4M. The entering temperature is 300K. (a) What CSTR reactor volume is necessary to achieve 80% conversion? (b) What conversion can be achieved in a 1000dm3 CSTR? What is the new exit temperature? (c) How would your answers to part (b) change, if the entering temperature of the feed were 280K ? Additional Information: HRx(300K)=3300cal/molCCPA=15cal/molCCPB=15cal/molCCPS=18cal/molCk(300K)=0.0005dm3/molminE=15,000cal/mol