drving By CSTR

F1CA=FA0(i+viX)CP=FA0(iCA+viCPX)=FA0(iCP+CPX) And the "friendly" form of the design equation becomes: ddT=FA0(iCP+CPX)rAHbUa(TTs) Must be coupled with mole balance equation: If the coolant temperature varies down the reactor we must add coolant balance: For an exothermic reaction (HR2)>0 2. CSTR with heat exchanger, UA (TaT). and large coolant flow ratc. XEB=HRx(FA0UA(TT0))+1CPi(TT0)T8 The elementary irreversible organic liquid phase reaction A+BC is carried out adiabatically in a flow reactor. An equimolar feed in A B enters at 27C, and the volumetric flow rate is 2dm3/s and CA0=0.1kmol/m3. a) Calculate the PFR and CSTR volume necessary to achieve 85% conversion. b) What is the maximum inlet temperature one could have so that the boiling point of the liquid (550 K) would not be exceeded even for complete conversion? c) Plot the conversion and temperature as function of PFR volume. d) Calculate the concentration achieved in one 500dm3 and in two 250 CSTRs in series. HA(273)=20kcal/mol,HB(273)=15kcal/mol,HC(273)=41 kcal/molCP,A=CPB=15cal/mol.K,CP,C=30cal/mol.K k=0.01dm3/mol.sat300K,E=10000cal/mol