The following elementary, irreversible liquid phase reaction is carried out adiabatically in a steady state CSTR of volume 10L. A+BP An equimolar feed of A and B is fed to the reactor at 300K with a volumetric flow rate of 2L/s and a total concentration of 6mol/L. Assume that CP is not a function of temperature. Additional information HA(273K)=10kcal/molHB(273K)=5kcal/molHP(273K)=20kcal/molCP,A=10cal/(molK)CP,B=12cal/(molK)CP,P=22cal/(molK)k(300K)=0.02L/(mols)EA=8000cal/mol Calculate the conversion and the operating temperature of the CSTR. [X=0.9,T=500K]