Distillation Modeling - Process Design Practice - Lecture Slides, Slides of Process Engineering

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

Typology: Slides

2012/2013

Uploaded on 08/21/2013

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Distillation Modeling

Distillation Fundamentals

•^

Understanding the Design Problem–^

Distillation Column Design vs. Distillation Column Rating

-^

Requires different tools, i.e. DISTWU and RADFRAC

-^

Remember you must

design

the columns for 100%

capacity, but

rate

them for 67% capacity

•^

DISTWU–^

This model uses the Winn-Underwood-Gilliland methodto estimate minimum reflux and number of stages

•^

RADFRAC–^

Rigorous distillation rating model for a given number ofstages, feed location and reflux ratio

Distillation Column Design

Using DISTWU in ASPEN Plus

Distillation Column Rating

Using RADFRAC in ASPEN Plus

Reactive Distillation

•^

Specifying Reactions and Chemistry–^

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

ASPEN

Plus

“REACTIONS”

and

“CHEMISTRY”

are

NOT

the same thing!

A + B

C + D

Reactive Distillation

•^

ASPEN Plus Input Forms

Defining the Reaction

RADFRAC Input Form

Reactive Distillation

•^

Balancing Kinetics and Hydraulics (Cont’d)

Tray Hold-up Specification

Troubleshooting RADFRAC

•^

Common Problems–^

Over specified column

-^

Not enough iterations

-^

Infeasible design specifications

-^

Operation below minimum reflux

-^

Wrong initialization routine

•^

Don’t be afraid to use the Help Menu!

•^

If you get stuck, Bob Kline or I can help!