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The elementary, irreversible, organic liquid-phase reaction A+BC is carried out adiabatically in a flow reactor. An equal molar feed in A and B enters at 27C, and the volumetric flow rate is 2dm3/s and CA0=0.1kmol/m3. Additional information: HA(273K)=20kcal/mol,HB(273K)=15kcal/mol,HC(273K)=41kcal/molCPA=CPB=15cal/molKCPC=30cal/molKk=0.01molsdm3at300KE=10,000cal/mol (d) Plot and then analyze the conversion and temperature profiles up to a PFR reactor volume of 10dm3 for the case when the reaction is reversible with KC=10m3/kmol at 450K. Plot the equilibrium conversion profile. How are the trends different than part (a)? CSTR (e) What is the CSTR volume necessary to achieve 90% conversion? BR (f) The reaction is next carried out in a 25dm3 batch reactor charged with NA0=10 moles. Plot the number of moles of A,NA, the conversion, and the temperature as a function of time