Reactive or catalytic distillation technology combines chemical synthesis steps with separations by distillation. This combination can lead to intensified, high-efficiency process systems with significant green engineering attributes. New applications and understanding have prompted growth in the use of reactive distillation for a variety of chemical syntheses, especially esterifications and etherifications involving oxygenated hydrocarbons. We describe several applications and the potential and tradeoffs for reactive distillation technology in the context of green engineering principles.
Fast and accurate distillation design requires a model that
significantly reduces the problem
size while accurately approximating a full-order distillation column
model. This collocation model
builds on the concepts of past collocation models for design of complex
real-world separation
systems. Two variable transformations make this method unique.
Polynomials cannot
accurately fit trajectories which flatten out. In columns, 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.
Furthermore, this model uses multiple collocation elements for a
column section, which is more
accurate than a single high-order collocation section.
We present applications for a collocation method for modeling
distillation columns that we
developed in a companion paper. We discuss implementation of the
model, including discussion
of the ASCEND system, which enables us to create complex models with
simple building blocks
and interactively learn to solve them. We first investigate
applying the model to compute
minimum reflux for a given separation task, exactly solving nonsharp
and approximately solving
sharp split minimum reflux problems. We next illustrate the use of
the collocation model to
optimize the design a single column capable of carrying out a
prescribed set of separation tasks.
The optimization picks the best column diameter and total number
of trays. It also picks the
feed tray for each of the prescribed separations.
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