Modeling and Simulation in Chemical Engineering

algebraic Analog Computer argument list array balance equation Batch Distillation calculated CALL INT Chapter coefficient column COMP Component mass balance composition condensate constant convergence DATA defined derivative section differential equations DYFLO dynamic END FIG enthalpy ENTHL equilibrium example exit stream F₁ feed first-order flow rate fluid FORTRAN function H₁ heat balance heat capacity Heat Exchanger heat flux heat transfer heat transfer coefficient HLDP holdup independent variable initial inlet integration section k₁ liquid loop LSTR main program mass balance mathematical model method mole balance mole fraction monomer obtained ordinary differential equations output P₁ P₂ partial differential equations particles phase polymer pressure problem procedure R₁ reaction rate reactor routine sensible heat shell side shown in Figure simulation solution solved specified stage steady-state step stream number STRM subroutine T₁ temperature thermowell tube side valve vapor stream vessel volume Y₁