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Some topics for Process Design Practice course are Mass integration, Advanced column design, Physical property prediction, Process risk assessment and Integration of design and control. This lecture includes: Distillation Modeling, Distillation Fundamentals, Mccabe-Thiele Diagram, Distillation Column Design, Distillation Column Rating, Tray Sizing and Rating, Reactive Distillation, Balancing Kinetics and Hydraulics, Aspen Plus Input Forms, Chemistry
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Distillation Column Design vs. Distillation Column Rating
-^
Requires different tools, i.e. DISTWU and RADFRAC
-^
Remember you must
the columns for 100%
capacity, but
them for 67% capacity
This model uses the Winn-Underwood-Gilliland methodto estimate minimum reflux and number of stages
Rigorous distillation rating model for a given number ofstages, feed location and reflux ratio
Using DISTWU in ASPEN Plus
Using RADFRAC in ASPEN Plus
Reactive
distillation
is
often
employed
in
equilibrium
systems to drive the reaction forward by removing oneof the components:
-^
In a Reactive Distillation column, each theoretical stagecan be considered as an individual CSTR
-^
From a kinetic standpoint, the design problem can beequated to the “CSTRs in Series” problem from yourreactor design course
-^
In
Plus
and
are
the same thing!
Defining the Reaction
RADFRAC Input Form
Tray Hold-up Specification
Over specified column
-^
Not enough iterations
-^
Infeasible design specifications
-^
Operation below minimum reflux
-^
Wrong initialization routine