“Chemical Engineering Equilibrium Separations” Lectures 15 1 22-31 Oct 2012.

Slides:



Advertisements
Similar presentations
DIP_10.ppt p. 1 Diseño Integrado de Procesos (Simulador) DIP 10.ppt Separation of a mixture of methanol + water Property Method Selection Model parameters.
Advertisements

Batch Distillation.
Absorption and Stripping
Structural Design and Separation Characteristic of Divided Wall Column by the Shortcut Method ● What is DWC ? -The DWC consists of one column in which.
Mass Transfer for 4 th Year Chemical Engineering Department Faculty of Engineering Cairo University.
A Selection of Chemical Engineering Problems Solved using Mathematica
CHEN 4460 – Process Synthesis, Simulation and Optimization Dr. Mario Richard Eden Department of Chemical Engineering Auburn University Lecture No. 4 –
Phase Equilibrium II - Two Component System. How many components and phases in this system? 2 components and 1 liquid phase Method to separate ethanol.
Process Modeling using Aspen Plus
Team 3: Robert Clifford, Patricia Firmin, Gen Liang, Rooma Raza
CENG 221 Lecture 4. Multi-component Distillation (4.5 h)
“Chemical Engineering Equilibrium Separations” Lectures 12 & Oct 2012.
Pharmaceutical API Process Development and Design
Michael Naas, Teddy Wescott, Andrew Gluck
Separation Trains Azeotropes
Advanced Distillation Column Modelling and Reactive Distillation
Batch Distillation John Ozbek Murat Ozkaya 11/25/08.
Separating Azeotropic Mixtures CHEN 4460 – Process Synthesis, Simulation and Optimization Dr. Mario Richard Eden Department of Chemical Engineering Auburn.
CHEN 4460 – Process Synthesis, Simulation and Optimization Dr. Mario Richard Eden Department of Chemical Engineering Auburn University Lecture No. 4 –
Distillation Underlying Principles of Distillation
EXAMPLES. UBAID UR REHMAN 2008-CHEM-19 ANAM ASIF 2008-CHEM-107 PRESENTED BY 2 CHEMICAL ENGINEERING DEPARTMENT, UET.
Designing a Separations Process Without VLE Data by Thomas Schafer - Koch Modular Process Systems, LLC This presentation utilizes as it’s example a problem.
1 Heteroazeotropic Batch Distillation Feasibility and Operation Stathis Skouras 7. May 2004 Department of Chemical Engineering, NTNU NTNU.
Unit Operations Lecture 19
Unit Operations Lecture 22 (continued)
Chemical Engineering Plant Design
Chemical Thermodynamics 2013/ th Lecture: Mixtures of Volatile Liquids Valentim M B Nunes, UD de Engenharia.
Lecture 15: Batch Distillation 1 Batch Distillation Total condenser Overhead vapor Boilup N 2 1 Distillation Reflux drum Rectifying section stages Stripping.
Approximate Methods for Multicomponent, Multistage Separations
SEQUENCING OF AZEOTROPIC DISTILLATION COLUMNS
Chemstations, Inc – Houston, TX – – Short Cut - Fenske-Underwood-Gilliland - Limited design, Rating Tower - Rigorous.
Dr Saad Al-ShahraniChE 334: Separation Processes Absorption of Dilute Mixtures  Graphical Equilibrium Stage Method for Trayed Tower  Consider the countercurrent-flow,
Unit Operations Lecture Nov McCabe-Thiele – AZ diagrams 2 Ethanol – Water Binary (1.013 bar):
McCabe Thiele Graphical Equilibrium-Stage
Ethylene glycol, HOCH 2 CH 2 OH, boils at 198 o C and melts at -13 o C. What happens to the melting point of water if you add antifreeze? Melting point.
ERT 313 BIOSEPARATION ENGINEERING DISTILLATION Prepared by: Miss Hairul Nazirah Abdul Halim.
Mass Transfer for 4 th Year Chemical Engineering Department Faculty of Engineering Cairo University.
The Simplest Phase Equilibrium Examples and Some Simple Estimating Rules Chapter 3.
Distillation... A Separation Method. Background Concepts - Definitions Vapor Pressure – Gas pressure created by the molecules of a liquid which have acquired.
CBE 417 “Unit Operations” 1 Instructor: David J. Dixon Chemical and Biological Engineering Department South Dakota School of Mines and Technology Fall.
“Chemical Engineering Equilibrium Separations”
CBE 417 “Unit Operations” Lecture: 3 7 Sep 2012.
“Chemical Engineering Equilibrium Separations”
8th International Symposium on Dynamics and Control of Process Systems (2007) Mexico/Cancun 1 NEW COLUMN CONFIGURATIONS FOR PRESSURE SWING BATCH DISTILLATION.
“Chemical Engineering Equilibrium Separations” Lectures Oct 2012.
Liquid-Vapor Phase Equilibrium Distillations will be performed in hood.
THERMODYNAMICS OF SEPARATION OPERATIONS
CBE 417 “Chemical Engineering Equilibrium Separations” 1 Lecture: 7 17 Sep 2012.
Dr Saad Al-ShahraniChE 201: Introduction to Chemical Engineering  Separation operations are subject to the conservation of mass  Separation of components.
CBE 417 “Unit Operations” 1 Lecture: 3 7 Sep 2012.
1 Classification and purification of Organic Compounds.
CHEMCAD User Meeting Berlin, September 2015
Noor Ahmad · Thomas Deskins · Lily Li · Shiv Patel
DISTILLATION DESIGN RIGOROUS METHODS.
Aspen Separation Unit Operations
A Review of Separation Topics
Process Equipment Design Distillation Columns
Team 3: Robert Clifford, Patricia Firmin, Gen Liang, Rooma Raza
Boiling Points - Distillations
Terry A. Ring Chemical Engineering University of Utah
ChEN 5253 Design II Chapter 13 Terry A. Ring University of Utah
Lecture 23: Review of Colligative Properties and Intro to Equilibrium
Aspen Separation Unit Operations
SEQUENCING OF AZEOTROPIC DISTILLATION COLUMNS
Separation Trains Azeotropes
Overall Review CHE 1008 Chapters 1-5, 6.4, 7, 9, 11, 12, 15.
Terry A. Ring Chemical Engineering University of Utah
Separation Columns (Distillation and absorption)
Hierarchy of Decisions
PROCESS AND PROCESS VARIABLE
Presentation transcript:

“Chemical Engineering Equilibrium Separations” Lectures Oct 2012

In-Class Problem 2 benzene (17 mol%) toluene (66 mol%) m-xylene (17 mol%) F = 100 kmol/s sat’d liquid 1 atm DSTWU barPi star [bar] ComponentTbp oC80.1 oC123 oC Benzene Toluene m-Xylene

In-Class Problem 3

4

5

6

7

8

Overview 9 AspenPlus: o Shortcut methods: DSTWU o Rigorous method: RADFRAC Efficiencies Introduction to multicomponent distillation (Chapter 9)

Homework Problem 10 benzene (17 mol%) toluene (66 mol%) m-xylene (17 mol%) F = 100 kmol/s sat’d liquid 1 atm X bz = 99 mol% X bz = 0.1 mol% DSTWU barPi star [bar] ComponentTbp oC80.1 oC123 oC Benzene Toluene m-Xylene

HWK Problem-molefrac specified 11

HWK Problem-molefrac specified 12

Overview 13 Review rigorous methods / RADFRAC Multicomponent systems: o Residue curves o DSTWU / RADFRAC o Rules of thumb Complex (Enhanced) distillation Column internals Batch distillation

14 Multicomponent Rigorous Methods Rigorous Methods: solution of stage by stage material balances, energy balances, and thermodynamic equilibrium equations.

AspenPlus: RADFRAC 15 Rigorous two- or three-phase fractionation for single columns. Models absorbers, strippers, reactive distillation, and so forth. RadFrac is a rigorous model for simulating all types of multistage vapor liquid fractionation operations. In addition to ordinary distillation, it can simulate: o absorption, reboiled absorption, stripping, reboiled stripping, extractive and azeotropic distillation

Rigorous Model 16

AspenPlus: RADFRAC 17 Rigorous two- or three-phase fractionation for single columns. Models absorbers, strippers, reactive distillation, and so forth. RadFrac is a rigorous model for simulating all types of multistage vapor liquid fractionation operations. In addition to ordinary distillation, it can simulate: o absorption, reboiled absorption, stripping, reboiled stripping, extractive and azeotropic distillation RadFrac is suitable for: o three phase systems, narrow boiling and wide boiling systems, systems exhibiting strong liquid phase nonideality RadFrac can detect and handle a free water phase or other second liquid phase anywhere in the column. You can decant free water from the condenser. RadFrac can handle solids on every stage. RadFrac can model columns where chemical reactions are occurring. Reactions can have fixed conversions, or they can be: o equilibrium, rate controlled, electrolytic RadFrac can model columns where two liquid phases exist and different chemical reactions occur in the two liquid phases. RadFrac can also model salt precipitation. RadFrac can operate in rating mode or design mode. With Aspen Rate-Based Distillation feature, RadFrac can perform rate-based distillation calculations (packed tower configurations).

Rating Mode 18

19

20

Design Mode 21

Rigorous Model 22

Multicomponent Methods 23 AspenPlus (methanol, ethanol, 1-propanol): Component P* i (64.5 oC) Keys MeOH1.013 bar EtOH Propanol AspenPlus Txy

“Residue” From Batch Distillation 24 Seader & Henley (2006)

Residue Curve Map 25

Residue Curve Map 26

Residue Curve Map 27

DSTWU 28 Z i = 1/3 R = 1.2 * R min MeOH recovery (dist.) = 99.9% EtOH recovery (dist.) = 0.1%

RADFRAC 29 Z i = 1/3 R = 5.2 N = 63 N F = 31 D = 33 kmol/h F = 100 kmol/h

Residue Curve Map 30

Plot Wizard 31

N F = 21 32

Set up Scheme 2 (1 st column only) 33 Run DSTWU Run RADFRAC Check performance

Questions? 34