2008 Spring Meeting & 4th Global Congress on Process Safety
(231d) Reduced Order Modeling of Rate-Based Distillation Columns
Authors
Welz, M. L. S. - Presenter, Sasol
Moller, K. - Presenter, University of Cape Town
Chakraborty, A. - Presenter, Sasol
This work presents an application of orthogonal collocation to a rigorous, nonequilibrium rate-based packed column. The low order model is constructed with a focus on the feed discontinuity, which is treated as a separate adiabatic flash.
An objective function is defined as the model solution to a combination of degrees of freedom. This definition allows for multiple solutions to a single separation specification to be found. The optimal solution can be subsequently found using an optimization routine. The construction of the objective function ensures that there is always a solution to the design problem.
The resulting low order model has potential use in for the design of distillation trains. If a full-order model is used, numerical difficulties ensue due to the resulting high degree of problem stiffness.