Consider an adiabatic CSTR operated to achieve the first-order conversion of species A to products. Assume constant density, dilute liquid-phase reaction. Important parameters describing the process are T=298K, Tr=8000K, pA=1000kJ/kg K, c=3.0×10−3kmol/m3, k=4.56×104kg m3, H=−10kJ/kmol, rho=1kg/m3. Write the time derivatives for the concentration of species A and the temperature of the reactor. Identify the parameters necessary to solve the problem, and compute their values. Be sure your units are consistent.
a. True
b. False