Fast and accurate distillation design requires a model that significan
tly reduces the problem size while accurately approximating a full-ord
er distillation column model. This collocation model builds on the con
cepts of past collocation models for design of complex real-world sepa
ration systems. Two variable transformations make this method unique.
Polynomials cannot accurately fit trajectories which flatten out. In c
olumns, flat sections occur in the middle of large column sections or
where concentrations go to 0 or 1. With an exponential transformation
of the tray number which maps zero to an infinite number of trays onto
the range 0-1, four collocation trays can accurately simulate a large
column section. With a hyperbolic tangent transformation of the mole
fractions, the model can simulate columns which reach high purities. F
urthermore, this model uses multiple collocation elements for a column
section, which is more accurate than a single high-order collocation
section.