DOF Analysis on a Distillation Process
In this simulation, a degree-of-freedom analysis is performed on a distillation process to determine whether the system has sufficient information to solve for the unknown variables. Use buttons to select the unit on which to do mass balances (distillation column, condenser, or reboiler) or to do a balance on the overall system. When “condenser” is selected, use buttons to select “partial condenser” or “total condenser”. Set the “total number of unknowns” with the slider; unknown variables are colored blue on the diagram and known variables are black. The known variables are selected randomly, and they change when you click the “new problem” button. Use buttons to select how species B is represented: as zB or as 1 – zA; the degree-of-freedom analysis is different for each representation. An explanation of the analysis is shown on the right. For zero degrees of freedom, the balances are solvable. The system is overspecified if it has more equations than unknowns and it is underspecified if it has more unknowns than equations. For a reboiler, the equilibrium ratio Kr, is known, and for a partial condenser the equilibrium ratio Kc is known. Temperatures and pressures are known for this analysis. Mass balances and phase equilibrium relations are solved to determine the unknown variables.
This simulation was made at the University of Colorado Boulder, Department of Chemical and Biological Engineering. Author: Rachael L. Baumann
View the source code for this simulation