Reactor Design within Excel Enabled by Rigorous Physical Properties and an Advanced Numerical Computation Package

Size: px
Start display at page:

Download "Reactor Design within Excel Enabled by Rigorous Physical Properties and an Advanced Numerical Computation Package"

Transcription

1 Reactor Design within Excel Enabled by Rigorous Physical Properties and an Advanced Numerical Computation Package Mordechai Shacham Department of Chemical Engineering Ben Gurion University of the Negev Beer-Sheva, Israel Michael B. Cutlip Department of Chemical Engineering University of Connecticut Storrs, CT, USA

2 Problem Solving in Chemical Engineering Mathematical Model Physical Properties Solution Algorithm Documentation

3 Chemical Engineer s Tools of Trade Calculation Documentation Properties Graphical Solution

4 Chemical Engineer s Problem Solution Techniques Analytical solutions, including Model simplification by neglecting less important terms Model manipulation to bring it into a solvable form Short-cut solution techniques Replacing the problem with a simpler one that can be solved Graphical solutions Trial and error solution techniques Numerical solution, including Computer language programming and debugging

5 Shortcomings of the Traditional Solution Techniques Manual and Graphical Solution Techniques Tedious, time consuming error prone process Oversimplification may lead to wrong results Highest precision is two decimal digits Time constraints prevent screening of large number of alternatives to find an optimal solution Computer Language Programming Requires experts in programming, numerical and optimization methods Tedious, time consuming error prone process

6 Modern Problem Solving Techniques Mathematical Model Physical Properties User Supplied Solution Algorithm Mathematical Software Package Documentation Using this approach the USER supplies the mathematical model and the physical properties and the package provides the numerical solution. Appropriate for small scale problems and when model flexibility is essential.

7 Modern Problem Solving Techniques Fogler H. S., An Appetizing Structure of Chemical Reaction Engineering for Undergraduates, Chem. Eng. Ed., 27(2), 110(1993)

8 Modern Problem Solving Techniques Mathematical Model Physical Properties Process Simulator Solution Algorithm Documentation Using this approach the USER provides only the process data. Appropriate for large scale problems.

9 Chemical Engineering Student s Tools of Trade Material and Energy Balances (Prentice- Hall textbook by Himmelblau, 2003) Thermodynamics (Prentice-Hall textbook by Kyle, 1999) Chemical Reaction Engineering (Prentice-Hall textbook by Fogler, 2004, Wiley-VCH textbook by Hagen, 2004) Process Dynamics and Control, Process Modeling and Numerical Methods Product and Process Design and Simulation

10 The use of POLYMATH throughout the ChE curriculum Chapters Coming next year in the 2 nd edition Basic Principles and Calculations, Thermodynamics, Fluid Mechanics, Heat transfer, Mass Transfer, Chemical Reaction Engineering Regression and Correlation of Data, Advanced Techniques in Problem Solving. Additional chapters: Separation Processes, Biotechnology, Process Dynamics and Control Conversion of POLYMATH models to Excel and MATLAB

11 Need for Spreadsheet-Based Calculations 287 Responses This nonprofit Educational Corporation is headquartered at the University of Texas at Austin.

12

13 Process Simulation Programs (Flowsheeting) in Organizations None 58.2% (163) Aspen+ 20% (56) Hysys 14.3% (40) SIMSCI Pro II 7.5% (21) ChemCAD 1.8% (5) gproms 1.4% (4) WINSIM 0.7% (2) Other 6.1% (17)

14 Extending the Use of Numerical Problem Solving By Practicing Engineers 100% of the engineers in the industry use spreadsheets (mainly Excel) while only a very small percentage use programs as Polymath, MATLAB and Aspen. Excel is inappropriate for complex numerical problem solving because of the need to convert variable names to cell addresses, difficulties in program documentation and unavailability of an ODE solver. Polymath 6.0, due to be released this fall, enables definition of the problem using the Polymath notation and syntax and conversion of the Polymath input into a well documented Excel worksheet. A new ODE solver for Excel is also provided.

15 The New Paradigm in Problem Solving Mathematical Model Physical Properties Aspen Properties Solution Algorithm Excel Polymath 6.0 Documentation

16 POLYMATH 6.0 Allows Easy Entry and Solution of Mathematical Problems using Numerical Analysis Capabilities Linear Equations - up to 264 simultaneous equations. Nonlinear Equations - up to 300 simultaneous nonlinear and 300 explicit algebraic equations Differential Equations - up to 300 simultaneous ordinary differential and 300 explicit algebraic equations Data analysis and Regression - up to 1200 data points with capabilities for linear, multiple linear, and nonlinear regressions with extensive statistics plus polynomial and spline fitting with interpolation and graphing capabilities NEW Automatic Migration of All Problems to Excel

17 POLYMATH A Long History in Engineering Computations

18 Aspen Properties Excel Calculator Pure component constants (MW, Normal boiling point). Vapor pressure at a specified temperature Pure component property at specified temperature and pressure Mixture properties for a specified mixture at given temperature and pressure Two and three phase flash, bubble and dew point calculations (enables solving simultaneous differential and algebraic equations, DAE)

19 Non-isothermal Reactor Design Problem Adiabatic operation will be modeled. 1 Fogler, H. S., Example 8-7, Elements of Chemical Reaction Engineering, 3rd Edition, Prentice-Hall, Upper Saddle River, NJ (1999)

20 Reactor Design Problem Model Equations Let A = acetone, B = ketene and C = methane, thus A B + C Mole Balances df dv A df dv B = ra; = ra and df C dv = r A Rate Law r = A kc A Stoichiometry C Energy Balance (Adiabatic Operation) A y P A = ; RT dt dv = y F A A = C F pa A + F F ( H + F B A B R C + pb F C )( r + A ) F C C pc

21 Reactor Design - Polymath Model Entry Physical properties are needed Note notation and syntax as in problem definition No need to reorder equations Model serves as documentation

22 Physical Properties The Traditional Approach

23 Physical Properties The Traditional Approach (2) Data and part of the calculations

24 Creation of a Physical Property Data File in Aspen Properties Physical Properties The New Approach

25 Specification of Components in Aspen Properties Physical Properties The New Approach

26 Specification of Property Method in Aspen Properties Physical Properties The New Approach

27 Saving Data File within Aspen Properties for Use in Excel

28 Provision of Physical Property Data in Excel by Aspen Properties Add-In Feed temperature and mole fractions CPA CPB CPC Copy to Polymath

29 Connection of Property Data to Polymath Program within Excel The variables T, P, ya (mole fraction of A), yb, and yc must be sent to the corresponding variable locations with the Aspen Properties area of the Excel worksheet. Additionally, the variables deltah (heat of reaction calculated from the enthalpies), CpA (heat capacity of A), CpB, and CpC must be made available in the Polymath coding for the solution of the differential equations.

30 Polymath Model With Aspen Properties Data

31 Export of Polymath Program to Excel (A single key press automatically migrates the problem.) Excel Formulas Documentation Documentation

32 Excel Formulas for the Reactor Problem Initial model set-up with Excel is a tedious and error prone process because of the need to convert variable names to cell addresses. This is practically impossible for a complex problem.

33 Connecting Data Information between Polymath and Aspen Properties Constant values are replaced by cell addresses from Aspen Properties

34 The Polymath ODE_Solver can then be used to solve the system of differential and explicit algebraic equations.

35 Note that as the temperature changes in the reactor, this new temperature is used in Aspen Properties to update the heat of reaction and the heat capacities within the equations used to solve the differential and algebraic equations. During the integration of the differential equations, the property values change with the temperature as the independent variable goes from 0 to 4.

36 The Polymath ODE_Solver automatically presents the results in a new sheet in the Excel workbook.

37 Columns of intermediate data can be identified for plotting in Excel.

38 These data columns can then be plotted with Excel. 40 Fogler Example Problem Molar Flow Rates, mol/s FA FB FC FB and FC coincide in this graph Reactor Volume, m3

39 Figure E8-7.1 from the Fogler textbook can also be generated from the intermediate data by using Excel. Fogler Example Temperature, K Conversion Excel Plot Volume, m3 Fogler Text Plot

40 Additional Typical Examples that Have Been Solved Utilizing the New Approach 1. Reactor Design Conversion of Nitrobenzene to Aniline in a Tubular Reactor Oxidation of O-Xylene to Phthalic Anhydride in a Tubular Reactor Batch Decomposition of Acetylated Castor Oil Semi-Batch Manufacture of Hexamethylenetriamine 2. Batch Distillation Separation of Methanol from Water in a Four Stage Column Multicomponent, Semi-Batch Steam Distillation 3. Steady State Absorption Column Design 4. Rigorous Heat Exchanger Design

41 SUMMARY This paper highlights the highlights the concepts necessary for advanced problem solving with Excel as enabled by Polymath and Aspen Properties. These are: Entry of basic problem in Polymath 6 with constant physical properties followed by export to Excel. Creation of a physical property data base within Aspen Properties followed by export to Excel via Aspen Properties Excel Add-In. Formulation of the problem within Excel that links the physical properties from Aspen Properties to the equations from Polymath. Use of the Polymath ODE_Solver Add-In to solve the problem within Excel. Generation of tabular and graphical outputs within Excel.

42 CONCLUSIONS Polymath and Aspen Properties now allow the solution of real-life, process design and related problems in a short time and with high precision, using Excel. Chemical engineering professionals can start using the combined Polymath -> Excel <- Aspen Properties capability immediately in solving real problems on the personal computer desktop.

43 CONCLUSIONS (Cont.) Chemical engineering students can begin using the combined Polymath -> Excel <- Aspen Properties capability for problem solving in their first engineering course of Material and Energy Balances. Students can continue to use the same approach throughout their CHEG curriculum and will carry this capability into their industrial practice.

44 Software References Aspen Properties is a product of AspenTech Excel is a product of Microsoft Corporation Polymath is a product of Polymath Software

Enabling Advanced Problem Solving in Spreadsheets with Access to Physical Property Data

Enabling Advanced Problem Solving in Spreadsheets with Access to Physical Property Data Enabling Advanced Problem Solving in Spreadsheets with Access to Physical Property Data Michael B. Cutlip, Professor of Chemical Engineering, University of Connecticut (speaker) michael.cutlip@uconn.edu

More information

Historical Perspective on Numerical Problem Solving

Historical Perspective on Numerical Problem Solving Historical Perspective on Numerical Problem Solving Mordechai Shacham Department of Chemical Engineering Ben Gurion University of the Negev Beer-Sheva, Israel Michael B. Cutlip Department of Chemical Engineering

More information

Combining Numerical Problem Solving with Access to Physical Property Data a New Paradigm in ChE Education

Combining Numerical Problem Solving with Access to Physical Property Data a New Paradigm in ChE Education Combining Numerical Problem Solving with Access to Physical Property Data a New Paradigm in ChE Education Michael B. Cutlip, Mordechai Shacham, and Michael Elly Dept. of Chemical Engineering, University

More information

What is "In" and What is "Out" in Engineering Problem Solving

What is In and What is Out in Engineering Problem Solving 18 th European Symposium on Computer Aided Process Engineering ESCAPE 18 Bertrand Braunschweig and avier Joulia (Editors) 008 Elsevier B.V./Ltd. All rights reserved. M. Shacham, M. B. Cutlip and N. Brauner,"What

More information

Enhancing Computer-Based Problem Solving Skills with a Combination of Software Packages

Enhancing Computer-Based Problem Solving Skills with a Combination of Software Packages 3420 Enhancing Computer-Based Problem Solving Sills with a Combination of Software Pacages Mordechai Shacham Dept. of Chemical Engineering, Ben Gurion University of the Negev Beer-Sheva 84105, Israel e-mail:

More information

THE PROCESS SIMULATION COURSE THE CULMINATION OF CORE UNDERGRADUATE COURSEWORK IN CHEMICAL ENGINEERING

THE PROCESS SIMULATION COURSE THE CULMINATION OF CORE UNDERGRADUATE COURSEWORK IN CHEMICAL ENGINEERING THE PROCESS SIMULATION COURSE THE CULMINATION OF CORE UNDERGRADUATE COURSEWORK IN CHEMICAL ENGINEERING Mordechai Shacham, Ben-Gurion University, Beer-Sheva, Israel Michael B. Cutlip, University of Connecticut,

More information

ACCESS AND UTILIZATION OF THE DIPPR PHYSICAL PROPERTY DATABASE IN CH. E. EDUCATION

ACCESS AND UTILIZATION OF THE DIPPR PHYSICAL PROPERTY DATABASE IN CH. E. EDUCATION ACCESS AND UTILIZATION OF THE DIPPR PHYSICAL PROPERTY DATABASE IN CH. E. EDUCATION Michael B. Cutlip, University of Connecticut, Storrs, CT Mordechai Shacham, Ben-Gurion Universi ty of the Negev, Beer-Sheva,

More information

Application of Mathematical Software Packages in Chemical Engineering Education DEMONSTRATION PROBLEMS

Application of Mathematical Software Packages in Chemical Engineering Education DEMONSTRATION PROBLEMS Application of Mathematical Software Packages in Chemical Engineering Education DEMONSTRATION PROBLEMS Sessions 16 and 116 ASEE Chemical Engineering Division Summer School University of Colorado - Boulder

More information

Selecting the Appropriate Numerical Software for a Chemical Engineering Course

Selecting the Appropriate Numerical Software for a Chemical Engineering Course Selecting the Appropriate Numerical Software for a Chemical Engineering Course Mordechai Shacham, shacham@bgumail.bgu.ac.il Chemical Engineering Department, Ben-Gurion University of the Negev, Beer-Sheva

More information

A Web based Library for Testing Performance of Numerical Software for Solving Nonlinear Algebraic Equations

A Web based Library for Testing Performance of Numerical Software for Solving Nonlinear Algebraic Equations A Web based Library for Testing Performance of Numerical Software for Solving Nonlinear Algebraic Equations M. Shacham a, N. Brauner b and M. B. Cutlip c a Dept. of Chemical Engineering, Ben Gurion University

More information

CONSIM - MS EXCEL BASED STUDENT FRIENDLY SIMULATOR FOR TEACHING PROCESS CONTROL THEORY

CONSIM - MS EXCEL BASED STUDENT FRIENDLY SIMULATOR FOR TEACHING PROCESS CONTROL THEORY CONSIM - MS EXCEL BASED STUDENT FRIENDLY SIMULATOR FOR TEACHING PROCESS CONTROL THEORY S. Lakshminarayanan, 1 Rao Raghuraj K 1 and S. Balaji 1 1 Department of Chemical and Biomolecular Engineering, 4 Engineering

More information

INTRODUCTION TO CHEMICAL ENGINEERING COMPUTING

INTRODUCTION TO CHEMICAL ENGINEERING COMPUTING INTRODUCTION TO CHEMICAL ENGINEERING COMPUTING BRUCE A. FINLÄYSON, PH.D. University of Washington Seattle, Washington iwiley- INTERSCIENCE A JOHN WILEY & SONS, INC., PUBLICATION Microsoft product screen

More information

Many practical problems in chemical engineering

Many practical problems in chemical engineering ChE classroom SOLVING A SYSTEM OF NONLINEAR ALGEBRAIC EQUATIONS You Only Get Error Messages What to do Next? Mordechai Shacham a and Neima Brauner b a Ben-Gurion University of the Negev Beer-Sheva 8405,

More information

Systems Engineering Spring Group Project #1: Process Flowsheeting Calculations for Acetic Anhydride Plant. Date: 2/25/00 Due: 3/3/00

Systems Engineering Spring Group Project #1: Process Flowsheeting Calculations for Acetic Anhydride Plant. Date: 2/25/00 Due: 3/3/00 10.551 Systems Engineering Spring 2000 Group Project #1: Process Flowsheeting Calculations for Acetic Anhydride Plant Date: 2/25/00 Due: 3/3/00 c Paul I. Barton, 14th February 2000 At our Nowhere City

More information

Web Solved Problems Web Example SP-8.1 Hydrodealkylation of Mesitylene in a PFR CH 3 H 2. m-xylene can also undergo hydrodealkylation to form toluene:

Web Solved Problems Web Example SP-8.1 Hydrodealkylation of Mesitylene in a PFR CH 3 H 2. m-xylene can also undergo hydrodealkylation to form toluene: Chapter 8 Multiple Reactions W8-1 Web Solved Problems Web Example SP-8.1 Hydrodealkylation of Mesitylene in a PFR The production of m-xylene by the hydrodealkylation of mesitylene over a Houdry Detrol

More information

A COLLECTION OF TEN NUMERICAL PROBLEMS IN CHEMICAL ENGINEERING SOLVED BY VARIOUS MATHEMATICAL SOFTWARE PACKAGES

A COLLECTION OF TEN NUMERICAL PROBLEMS IN CHEMICAL ENGINEERING SOLVED BY VARIOUS MATHEMATICAL SOFTWARE PACKAGES IN CHEMICAL ENGINEERING SOLVED BY VARIOUS MATHEMATICAL SOFTWARE PACKAGES Michael B. Cutlip, Department of Chemical Engineering, Box U-222, University of Connecticut, Storrs, CT 06269-3222 (mcutlip@uconnvm.uconn.edu)

More information

Teaching Assistant: Tracy Bucholz CPE office hours: M, W, F 8:30-9:30am

Teaching Assistant: Tracy Bucholz CPE office hours: M, W, F 8:30-9:30am ChE 317: INTRODUCTION TO CHEMICAL ENGINEERING ANALYSIS T. Th 8-9:30 CPE 2.218 Personnel Contact Information Course Instructor: Prof. Lynn Loo lloo@che.utexas.edu CPE 4.422 471-6300 office hours: T, Th

More information

Problem Solving in Chemical Engineering with Numerical Methods

Problem Solving in Chemical Engineering with Numerical Methods Problem Solving in Chemical Engineering with Numerical Methods Michael B. Cutlip University of Connecticut Mordechai Shacham Ben-Gurion University of the Negev To join a Prentice Hall PTR Internet mailing

More information

Linear Algebra is Your Friend: Least Squares Solutions to Overdetermined Linear Systems

Linear Algebra is Your Friend: Least Squares Solutions to Overdetermined Linear Systems Linear Algebra is Your Friend: Least Squares Solutions to Overdetermined Linear Systems R. E. Babcock, Mark E. Arnold Department of Chemical Engineering and Department of Mathematical Sciences Fayetteville,

More information

1. Open polymath: 2. Go to Help, Contents F1 or Press F1

1. Open polymath: 2. Go to Help, Contents F1 or Press F1 Polymath Tutorial Process Fluid Transport 1. Open polymath: 2. Go to Help, Contents F1 or Press F1 1 3. Read the section titled Introduction to Polymath both getting started and Variables and expressions

More information

Appendix A Course Syllabi Appendix A: Syllabi. Engineering Physics. Bachelor of Science in Engineering Physics. Self-Study Report

Appendix A Course Syllabi Appendix A: Syllabi. Engineering Physics. Bachelor of Science in Engineering Physics. Self-Study Report Appendix A Course Syllabi Appendix A: Syllabi Engineering Physics Bachelor of Science in Engineering Physics Self-Study Report New Mexico State University 159 Chemical Engineering Courses Chemical Engineering

More information

SIMULIS THERMODYNAMICS

SIMULIS THERMODYNAMICS 2007 AIChE Annual Meeting Salt Lake City, Utah #459e CAPE-OPEN Thermodynamic & Physical Properties Interface (TD002) SIMULIS THERMODYNAMICS A CAPE-OPEN COMPLIANT FRAMEWORK FOR USERS AND DEVELOPERS Olivier

More information

Accuracy of Mathematical Model with Regard to Safety Analysis of Chemical Reactors*

Accuracy of Mathematical Model with Regard to Safety Analysis of Chemical Reactors* Accuracy of Mathematical Model with Regard to Safety Analysis of Chemical Reactors* A. MOLNÁR, J. MARKOŠ, and Ľ. JELEMENSKÝ Department of Chemical and Biochemical Engineering, Faculty of Chemical and Food

More information

ChemSep Case Book: Handling Missing Components

ChemSep Case Book: Handling Missing Components ChemSep Case Book: Handling Missing Components Ross Taylor and Harry Kooijman In their book Conceptual Design of Distillation Systems M.F. Doherty and M.F. Malone (McGraw-Hill, 2001) describe a process

More information

4 th Edition Chapter 9

4 th Edition Chapter 9 Insert Page 547A 4 th Edition Chapter 9 In summary, if any one of the following three things had not occurred the explosion would not have happened. 1. Tripled production 2. Heat exchanger failure for

More information

AC : A MODULE FOR TEACHING BATCH OPERATIONS

AC : A MODULE FOR TEACHING BATCH OPERATIONS AC 2010-726: A MODULE FOR TEACHING BATCH OPERATIONS Richard Turton, West Virginia University Richard Turton received his B.S. degree from the University of Nottingham and his M.S. and Ph.D. degrees from

More information

Theoretical Models of Chemical Processes

Theoretical Models of Chemical Processes Theoretical Models of Chemical Processes Dr. M. A. A. Shoukat Choudhury 1 Rationale for Dynamic Models 1. Improve understanding of the process 2. Train Plant operating personnel 3. Develop control strategy

More information

Application of Mathematical Software Packages in Chemical Engineering Education ASSIGNMENT PROBLEMS

Application of Mathematical Software Packages in Chemical Engineering Education ASSIGNMENT PROBLEMS Application of Mathematical Software Packages in Chemical Engineering Education ASSIGNMENT PROBLEMS Sessions 16 and 116 ASEE Chemical Engineering Division Summer School University of Colorado - Boulder

More information

CHE 404 Chemical Reaction Engineering. Chapter 8 Steady-State Nonisothermal Reactor Design

CHE 404 Chemical Reaction Engineering. Chapter 8 Steady-State Nonisothermal Reactor Design Textbook: Elements of Chemical Reaction Engineering, 4 th Edition 1 CHE 404 Chemical Reaction Engineering Chapter 8 Steady-State Nonisothermal Reactor Design Contents 2 PART 1. Steady-State Energy Balance

More information

Integrated Knowledge Based System for Process Synthesis

Integrated Knowledge Based System for Process Synthesis 17 th European Symposium on Computer Aided Process Engineering ESCAPE17 V. Plesu and P.S. Agachi (Editors) 2007 Elsevier B.V. All rights reserved. 1 Integrated Knowledge Based System for Process Synthesis

More information

CHE 404 Chemical Reaction Engineering. Chapter 8 Steady-State Nonisothermal Reactor Design

CHE 404 Chemical Reaction Engineering. Chapter 8 Steady-State Nonisothermal Reactor Design Textbook: Elements of Chemical Reaction Engineering, 4 th Edition 1 CHE 404 Chemical Reaction Engineering Chapter 8 Steady-State Nonisothermal Reactor Design Contents 2 PART 1. Steady-State Energy Balance

More information

STEAMEST: A Software Tool for Estimation of Physical Properties of Water and Steam

STEAMEST: A Software Tool for Estimation of Physical Properties of Water and Steam 226 JOURNAL OF SOFTWARE, VOL. 4, NO. 3, MAY 2009 STEAMEST: A Software Tool for Estimation of Physical Properties of Water and Steam Muhammad Faheem Department of Chemical Engineering, University of Engineering

More information

POLYMATH SOLUTIONS TO THE CHEMICAL ENGINEERING DEMONSTRATION PROBLEM SET

POLYMATH SOLUTIONS TO THE CHEMICAL ENGINEERING DEMONSTRATION PROBLEM SET Sessions 16 and 116 POLYMATH SOLUTIONS TO THE CHEMICAL ENGINEERING DEMONSTRATION PROBLEM SET Mathematical Software - Sessions 16 and 116* Michael B. Cutlip, Department of Chemical Engineering, Box U-3222,

More information

Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09)

Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09) Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09) In this session you will learn how to create a stoichiometric reactor model

More information

Aspen Dr. Ziad Abuelrub

Aspen Dr. Ziad Abuelrub Aspen Plus Lab Pharmaceutical Plant Design Aspen Dr. Ziad Abuelrub OUTLINE 1. Introduction 2. Getting Started 3. Thermodynamic Models & Physical Properties 4. Pressure Changers 5. Heat Exchangers 6. Flowsheet

More information

ChE 344 Winter 2013 Final Exam + Solution. Open Course Textbook Only Closed everything else (i.e., Notes, In-Class Problems and Home Problems

ChE 344 Winter 2013 Final Exam + Solution. Open Course Textbook Only Closed everything else (i.e., Notes, In-Class Problems and Home Problems ChE 344 Winter 03 Final Exam + Solution Thursday, May, 03 Open Course Textbook Only Closed everything else (i.e., Notes, In-Class Problems and Home Problems Name Honor Code (Please sign in the space provided

More information

Aspen Plus PFR Reactors Tutorial using Styrene with Pressure Drop Considerations By Robert P. Hesketh and Concetta LaMarca Spring 2005

Aspen Plus PFR Reactors Tutorial using Styrene with Pressure Drop Considerations By Robert P. Hesketh and Concetta LaMarca Spring 2005 Aspen Plus PFR Reactors Tutorial using Styrene with Pressure Drop Considerations By Robert P. Hesketh and Concetta LaMarca Spring 2005 In this laboratory we will incorporate pressure-drop calculations

More information

Chemical Reaction Engineering (CRE) Education: From the Era of Slide Rule to the Digital Age

Chemical Reaction Engineering (CRE) Education: From the Era of Slide Rule to the Digital Age Chemical Reaction Engineering (CRE) Education: From the Era of Slide Rule to the Digital Age H. Scott Fogler, University of Michigan Michael B. Cutlip, University of Connecticut Abstract The complexity

More information

Pressure Swing Distillation with Aspen Plus V8.0

Pressure Swing Distillation with Aspen Plus V8.0 Pressure Swing Distillation with Aspen Plus V8.0 1. Lesson Objectives Aspen Plus property analysis RadFrac distillation modeling Design Specs NQ Curves Tear streams Understand and overcome azeotrope Select

More information

Ammonia Synthesis with Aspen Plus V8.0

Ammonia Synthesis with Aspen Plus V8.0 Ammonia Synthesis with Aspen Plus V8.0 Part 1 Open Loop Simulation of Ammonia Synthesis 1. Lesson Objectives Become comfortable and familiar with the Aspen Plus graphical user interface Explore Aspen Plus

More information

All rights reserved. Armando B. Corripio, PhD, PE Flash Distillation Flash Drum Variables and Specifications... 2

All rights reserved. Armando B. Corripio, PhD, PE Flash Distillation Flash Drum Variables and Specifications... 2 Flash Distillation All rights reserved. Armando B. Corripio, PhD, PE. 2013 Contents Flash Distillation... 1 1 Flash Drum Variables and Specifications... 2 2 Flash Drum Balances and Equations... 4 2.1 Equilibrium

More information

Unit operations are ubiquitous in any chemical process. Equilibrium-Staged Separations using Matlab and Mathematica. ChE class and home problems

Unit operations are ubiquitous in any chemical process. Equilibrium-Staged Separations using Matlab and Mathematica. ChE class and home problems ChE class and home problems The object of this column is to enhance our readers collections of interesting and novel problems in chemical engineering. Problems of the type that can be used to motivate

More information

Thermodynamics revisited

Thermodynamics revisited Thermodynamics revisited How can I do an energy balance for a reactor system? 1 st law of thermodynamics (differential form): de de = = dq dq--dw dw Energy: de = du + de kin + de pot + de other du = Work:

More information

On the Necessary and Sufficient to Efficient Use of Software in the Teaching of Chemical Engineering

On the Necessary and Sufficient to Efficient Use of Software in the Teaching of Chemical Engineering ; Vol. 7, No. 3; 013 ISSN 1913-1844 E-ISSN 1913-185 Published by Canadian Center of Science and Education On the Necessary and Sufficient to Efficient Use of Software in the Teaching of Chemical Engineering

More information

AspenTech: VAPOR PRESSURES

AspenTech: VAPOR PRESSURES AspenTech: VAPOR PRESSURES Technical Memo No. XX-1 Subject: Vapor pressure interpolation error analysis To: Ms. Sam K. Safobeen Submitted by: Student 2 Date: May 11, 2010 Summary: I have compiled vapor

More information

Review of Chemical Equilibrium Introduction

Review of Chemical Equilibrium Introduction Review of Chemical Equilibrium Introduction Copyright c 2015 by Nob Hill Publishing, LLC This chapter is a review of the equilibrium state of a system that can undergo chemical reaction Operating reactors

More information

Introduction to the course ``Theory and Development of Reactive Systems'' (Chemical Reaction Engineering - I)

Introduction to the course ``Theory and Development of Reactive Systems'' (Chemical Reaction Engineering - I) Introduction to the course ``Theory and Development of Reactive Systems'' (Chemical Reaction Engineering - I) Prof. Gabriele Pannocchia Department of Civil and Industrial Engineering (DICI) University

More information

Chapter 4. Problem SM.7 Ethylbenzene/Styrene Column

Chapter 4. Problem SM.7 Ethylbenzene/Styrene Column Background Chapter 4. Problem SM.7 Ethylbenzene/Styrene Column In Problem SM.6 of the HYSYS manual, a modified form of successive substitution, called the Wegstein method, was used to close the material

More information

Example 8: CSTR with Multiple Solutions

Example 8: CSTR with Multiple Solutions Example 8: CSTR with Multiple Solutions This model studies the multiple steady-states of exothermic reactions. The example is from Parulekar (27) which in turn was modified from one by Fogler (1999). The

More information

Review of Chemical Equilibrium Introduction

Review of Chemical Equilibrium Introduction Review of Chemical Equilibrium Introduction Copyright c 2015 by Nob Hill Publishing, LLC This chapter is a review of the equilibrium state of a system that can undergo chemical reaction Operating reactors

More information

Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati

Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module - 5 Distillation Lecture - 5 Fractional Distillation Welcome to the

More information

Athena Visual Software, Inc. 1

Athena Visual Software, Inc. 1 Athena Visual Studio Visual Kinetics Tutorial VisualKinetics is an integrated tool within the Athena Visual Studio software environment, which allows scientists and engineers to simulate the dynamic behavior

More information

MATHCAD SOLUTIONS TO THE CHEMICAL ENGINEERING PROBLEM SET

MATHCAD SOLUTIONS TO THE CHEMICAL ENGINEERING PROBLEM SET MATHCA SOLUTIONS TO THE CHEMICAL ENGINEERING PROBLEM SET Mathematical Software Session John J. Hwalek, epartment of Chemical Engineering University of Maine, Orono, Me 4469-5737 (hwalek@maine.maine.edu)

More information

Chemical Kinetics I: The Dry Lab. Up until this point in our study of physical chemistry we have been interested in

Chemical Kinetics I: The Dry Lab. Up until this point in our study of physical chemistry we have been interested in Chemical Kinetics I: The Dry Lab Up until this point in our study of physical chemistry we have been interested in equilibrium properties; now we will begin to investigate non-equilibrium properties and

More information

THERMODYNAMIC ANALYSIS OF MULTICOMPONENT DISTILLATION-REACTION PROCESSES FOR CONCEPTUAL PROCESS DESIGN

THERMODYNAMIC ANALYSIS OF MULTICOMPONENT DISTILLATION-REACTION PROCESSES FOR CONCEPTUAL PROCESS DESIGN THERMODYNAMIC ANALYSIS OF MULTICOMPONENT DISTILLATION-REACTION PROCESSES FOR CONCEPTUAL PROCESS DESIGN Oliver Ryll, Sergej Blagov 1, Hans Hasse Institute of Thermodynamics and Thermal Process Engineering,

More information

Modeling of a Fluid Catalytic Cracking (FCC) Riser Reactor

Modeling of a Fluid Catalytic Cracking (FCC) Riser Reactor Modeling of a Fluid Catalytic Cracking (FCC) Riser Reactor Dr. Riyad Ageli Mahfud Department of Chemical Engineering- Sabrattah Zawia University Abstract: Fluid catalytic cracking (FCC) is used in petroleum

More information

A First Course on Kinetics and Reaction Engineering. Class 20 on Unit 19

A First Course on Kinetics and Reaction Engineering. Class 20 on Unit 19 A First Course on Kinetics and Reaction Engineering Class 20 on Unit 19 Part I - Chemical Reactions Part II - Chemical Reaction Kinetics Where We re Going Part III - Chemical Reaction Engineering A. Ideal

More information

MULTI-LOOP CONTROL STRUCTURE FOR DIVIDING-WALL DISTILLATION COLUMNS. Abstract. Introduction

MULTI-LOOP CONTROL STRUCTURE FOR DIVIDING-WALL DISTILLATION COLUMNS. Abstract. Introduction MULTI-LOOP CONTROL STRUCTURE FOR DIVIDING-WALL DISTILLATION COLUMNS Salvador Tututi-Avila, Center for Biotechnology and Interdisciplinary Studies, Rensselaer Polytechnic Institute, Troy, NY, Arturo Jiménez-Gutiérrez,

More information

Combining HAZOP with Dynamic Process Model Development for Safety Analysis

Combining HAZOP with Dynamic Process Model Development for Safety Analysis Combining HAZOP with Dynamic Process Model Development for Safety Analysis Shimon Eisenberg a, Mordechai Shacham a and Neima Brauner b a Dept. Chem. Eng., Ben-Gurion University Beer-Sheva, Israel b School

More information

Introduction to the Problem-Solving Methodology (PSM)

Introduction to the Problem-Solving Methodology (PSM) Problem Name: Problem Description: Date: P01 Simple Reactor Introduction to the Problem-Solving Methodology (PSM) Your Name: Problem Session Objectives To learn the five stages of the problem solving methodology.

More information

Enhancing Core Chemical Engineering Courses with Computationally-Intense Course Modules

Enhancing Core Chemical Engineering Courses with Computationally-Intense Course Modules Paper ID #21689 Enhancing Core Chemical Engineering Courses with Computationally-Intense Course Modules Dr. Kevin D. Dahm, Rowan University Kevin Dahm is a Professor of Chemical Engineering at Rowan University.

More information

University of Texas-Austin - Integration of Computing

University of Texas-Austin - Integration of Computing University of Texas-Austin - Integration of Computing During 2001-2002 the Department of Chemical Engineering at UT-Austin revamped the computing thread in its curriculum in order to strengthen student

More information

Getting started with BatchReactor Example : Simulation of the Chlorotoluene chlorination

Getting started with BatchReactor Example : Simulation of the Chlorotoluene chlorination Getting started with BatchReactor Example : Simulation of the Chlorotoluene chlorination 2011 ProSim S.A. All rights reserved. Introduction This document presents the different steps to follow in order

More information

Chemical Engineering 140. Chemical Process Analysis C.J. Radke Tentative Schedule Fall 2013

Chemical Engineering 140. Chemical Process Analysis C.J. Radke Tentative Schedule Fall 2013 Chemical Process Analysis C.J. Radke Tentative Schedule Fall 2013 Week 0 *8/30 1. Definition of Chemical Engineering: flow sheet, reactor trains and separation processes, raw materials, power production

More information

Business. Final Exam Review. Competencies. Schedule Today. Most missed on Exam 3. Review Exam #3

Business. Final Exam Review. Competencies. Schedule Today. Most missed on Exam 3. Review Exam #3 Business Final Exam Review Online course evaluation (19/32 = 59%) Counts as a homework assignment (by Thurs) Professional program application Past due! Case study due today by 5 pm Leadership evaluation

More information

DISTILLATION. Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation

DISTILLATION. Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation 25 DISTILLATION Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation Distillation refers to the physical separation of a mixture into two or more fractions that have different

More information

Determination of Density 1

Determination of Density 1 Introduction Determination of Density 1 Authors: B. D. Lamp, D. L. McCurdy, V. M. Pultz and J. M. McCormick* Last Update: February 1, 2013 Not so long ago a statistical data analysis of any data set larger

More information

Ms. Sally Richards, Co-op Program Manager Embry-Riddle Aeronautical University, Daytona Beach, Florida

Ms. Sally Richards, Co-op Program Manager Embry-Riddle Aeronautical University, Daytona Beach, Florida To: From: Ms. Sally Richards, Co-op Program Manager Embry-Riddle Aeronautical University, Daytona Beach, Florida 32114-3900 Gianluca Puliti, Research Assistant - Aerospace and Mechanical Engineering University

More information

CHEMICAL REACTION ENGINEERING

CHEMICAL REACTION ENGINEERING CHEMICL RECTION ENGINEERING Unit 5 nalysis of reactor DT Collection and analysis of rate data Batch reactor for homogenous and heterogeneous reactions measurement during the unsteady-state operation Differential

More information

Use of Differential Equations In Modeling and Simulation of CSTR

Use of Differential Equations In Modeling and Simulation of CSTR Use of Differential Equations In Modeling and Simulation of CSTR JIRI VOJTESEK, PETR DOSTAL Department of Process Control, Faculty of Applied Informatics Tomas Bata University in Zlin nám. T. G. Masaryka

More information

Thermodynamics and Rate Processes. D.Kunzru Dept. of Chemical Engineering I.I.T.Kanpur

Thermodynamics and Rate Processes. D.Kunzru Dept. of Chemical Engineering I.I.T.Kanpur Thermodynamics and Rate Processes D.Kunzru Dept. of Chemical Engineering I.I.T.Kanpur Importance of Chemical Reaction Engineering chemical reactor is usually the heart of any process traditional applications:

More information

Vapor-liquid equilibrium

Vapor-liquid equilibrium Vapor-liquid equilibrium From Wikipedia, the free encyclopedia Vapor-liquid equilibrium, abbreviated as VLE by some, is a condition where a liquid and its vapor (gas phase) are in equilibrium with each

More information

Digital Processing of Noise Experimental Sorption Data using Savitzky-Golay filter

Digital Processing of Noise Experimental Sorption Data using Savitzky-Golay filter Digital Processing of Noise Experimental Sorption Data using Savitzky-Golay filter Vladimír Hanta 1, Jaroslav Poživil 1, Karel Friess 2 Department of Computing and Control Engineering 1, Department of

More information

Exam 1 Chemical Reaction Engineering 26 February 2001 Closed Book and Notes

Exam 1 Chemical Reaction Engineering 26 February 2001 Closed Book and Notes Exam 1 Chemical Reaction Engineering 26 February 21 Closed Book and Notes (2%) 1. Derive the unsteady-state mole balance for a chemical species A for a packed bed reactor using the following steps: a)

More information

Exploring Excel spreadsheets in the teaching and learning of certain concepts of Statistical physics and Thermodynamics

Exploring Excel spreadsheets in the teaching and learning of certain concepts of Statistical physics and Thermodynamics Exploring Excel spreadsheets in the teaching and learning of certain concepts of Statistical physics and Thermodynamics Ionel Grigore 1,2, Cristina Miron 1, Emil-Stefan Barna 1 (1) Faculty of Physics,

More information

Computer Aided Design Module for a Binary Distillation Column

Computer Aided Design Module for a Binary Distillation Column Computer Aided Design Module for a Binary Distillation Column K. R. Onifade Department of Chemical Engineering, Federal University of Technology Minna, Nigeria Abstract A Computer Aided Design (CAD) module

More information

Physical Modeling of Hybrid Systems with Rand Model Designer

Physical Modeling of Hybrid Systems with Rand Model Designer Physical Modeling of Hybrid Systems with Rand Model Designer D. Inihov,* Y. Kolesov,** Y. Senichenkov*** *MvSoft, Moscow, Russia, (e-mail: inihov@mail.ru) **R F C A, Moscow, Russia (e-mail: ybk2@mail.ru)

More information

August 7, 2007 NUMERICAL SOLUTION OF LAPLACE'S EQUATION

August 7, 2007 NUMERICAL SOLUTION OF LAPLACE'S EQUATION August 7, 007 NUMERICAL SOLUTION OF LAPLACE'S EQUATION PURPOSE: This experiment illustrates the numerical solution of Laplace's Equation using a relaxation method. The results of the relaxation method

More information

Modeling and Simulation of Temperature Profiles in a Reactive Distillation System for Esterification of Acetic Anhydride with Methanol

Modeling and Simulation of Temperature Profiles in a Reactive Distillation System for Esterification of Acetic Anhydride with Methanol Modeling and Simulation of Temperature Profiles in a Reactive Distillation System for Esterification of Acetic Anhydride with Methanol N.Asiedu *, D.Hildebrandt *, D.Glasser * Centre of Material and Process

More information

Chabot College Fall Course Outline for Mathematics 25 COMPUTATIONAL METHODS FOR ENGINEERS AND SCIENTISTS

Chabot College Fall Course Outline for Mathematics 25 COMPUTATIONAL METHODS FOR ENGINEERS AND SCIENTISTS Chabot College Fall 2010 Course Outline for Mathematics 25 COMPUTATIONAL METHODS FOR ENGINEERS AND SCIENTISTS Catalog Description: MTH 25 - Computational Methods for Engineers and Scientists 3.00 units

More information

In The Name Of God. Ali Hashempour. M.Sc. Student at School of Chemical Engineering, College of Engineering, University of Tehran, Tehran, Iran.

In The Name Of God. Ali Hashempour. M.Sc. Student at School of Chemical Engineering, College of Engineering, University of Tehran, Tehran, Iran. In The Name Of God Ali Hashempour M.Sc. Student at School of Chemical Engineering, College of Engineering,, Tehran, Iran. +98 910 876 3444 Ali.hashempour@ut.ac.ir Ali.hashempour71@gmail.com Research Interests

More information

Introduction to Chemical Engineering Computing, 2 nd edition, Bruce A. Finlayson, Wiley (2012)

Introduction to Chemical Engineering Computing, 2 nd edition, Bruce A. Finlayson, Wiley (2012) Introduction to Chemical Engineering Computing, 2 nd edition, Bruce A. Finlayson, Wiley (2012) The following web sites can be used to obtain material from Wiley. It includes the keys to the problems (useful

More information

INTEGRATED PROCESS FOR γ-butyrolactone PRODUCTION

INTEGRATED PROCESS FOR γ-butyrolactone PRODUCTION U.P.B. Sci. Bull., Series B, Vol. 76, Iss. 3, 214 ISSN 1454 2331 INTEGRATED PROCESS FOR γ-butyrolactone PRODUCTION Ahtesham JAVAID 1, Costin Sorin BILDEA 2 An integrated process for the production of γ-butyrolactone

More information

A First Course on Kinetics and Reaction Engineering Example 14.3

A First Course on Kinetics and Reaction Engineering Example 14.3 Example 14.3 Problem Purpose This problem illustrates differential analysis using data from a differentially operated PFR. Problem Statement The isomerization of cyclopropane, equation (1), was known from

More information

Aggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems

Aggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems Aggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems Ravindra S. Kamath 1, Ignacio E. Grossmann 1,*, and Lorenz T. Biegler 1 1 Chemical Engineering Department,

More information

1. (25 points) C 6 H O 2 6CO 2 + 7H 2 O C 6 H O 2 6CO + 7H 2 O

1. (25 points) C 6 H O 2 6CO 2 + 7H 2 O C 6 H O 2 6CO + 7H 2 O MEEBAL Exam 2 November 2013 Show all work in your blue book. Points will be deducted if steps leading to answers are not shown. No work outside blue books (such as writing on the flow sheets) will be considered.

More information

CAPE-OPEN and Simulis Thermodynamics enable you to use rigorous thermodynamics in MATLAB

CAPE-OPEN and Simulis Thermodynamics enable you to use rigorous thermodynamics in MATLAB Alain VACHER Stratège Bâtiment A BP 2738 F-31312 LABEGE Cedex FRANCE www.prosim.net Dr Michel PONS CAPE-OPEN Laboratories Network 32 rue Raulin F-69007 LYON FRANCE www.colan.org CAPE-OPEN and Simulis Thermodynamics

More information

Short-cut distillation columns based on orthogonal polynomials of a discrete variable

Short-cut distillation columns based on orthogonal polynomials of a discrete variable Short-cut distillation columns based on orthogonal polynomials of a discrete variable Peter Lory Institut für Wirtschaftsinformatik, Universität Regensburg, D 93040 Regensburg, Germany Dedicated to Professor

More information

PHEN 612 SPRING 2008 WEEK 1 LAURENT SIMON

PHEN 612 SPRING 2008 WEEK 1 LAURENT SIMON PHEN 612 SPRING 2008 WEEK 1 LAURENT SIMON Chapter 1 * 1.1 Rate of reactions r A A+B->C Species A, B, and C We are interested in the rate of disappearance of A The rate of reaction, ra, is the number of

More information

A First Course on Kinetics and Reaction Engineering Unit 2. Reaction Thermochemistry

A First Course on Kinetics and Reaction Engineering Unit 2. Reaction Thermochemistry Unit 2. Reaction Thermochemistry Overview This course is divided into four parts, I through IV. Part I reviews some topics related to chemical reactions that most students will have encountered in previous

More information

CHAPTER FIVE REACTION ENGINEERING

CHAPTER FIVE REACTION ENGINEERING 1 CHAPTER FIVE REACTION ENGINEERING 5.1. Determination of Kinetic Parameters of the Saponification Reaction in a PFR 5.3. Experimental and Numerical Determination of Kinetic Parameters of the Saponification

More information

بسمه تعالي کنترل صنعتي 2 دکتر سید مجید اسما عیل زاده گروه کنترل دانشکده مهندسي برق دانشگاه علم و صنعت ایران پاییس 90

بسمه تعالي کنترل صنعتي 2 دکتر سید مجید اسما عیل زاده گروه کنترل دانشکده مهندسي برق دانشگاه علم و صنعت ایران پاییس 90 بسمه تعالي کنترل صنعتي 2 دکتر سید مجید اسما عیل زاده گروه کنترل دانشکده مهندسي برق دانشگاه علم و صنعت ایران پاییس 90 Techniques of Model-Based Control By Coleman Brosilow, Babu Joseph Publisher : Prentice

More information

TEACH YOURSELF THE BASICS OF ASPEN PLUS

TEACH YOURSELF THE BASICS OF ASPEN PLUS TEACH YOURSELF THE BASICS OF ASPEN PLUS TEACH YOURSELF THE BASICS OF ASPEN PLUS RALPH SCHEFFLAN Chemical Engineering and Materials Science Department Stevens Institute of Technology A JOHN WILEY & SONS,

More information

(1) This reaction mechanism includes several undesired side reactions that produce toluene and benzene:

(1) This reaction mechanism includes several undesired side reactions that produce toluene and benzene: HYSYS Multiple Reactions - Styrene Prepared by Robert P. Hesketh Spring 005 Styrene Reactor System You have been studying how to use HYSYS using the example of a Styrene reactor system. In this session

More information

Pure Component Equations

Pure Component Equations Pure Component Equations Fitting of Pure Component Equations DDBSP - Dortmund Data Bank Software Package DDBST Software & Separation Technology GmbH Marie-Curie-Straße 10 D-26129 Oldenburg Tel.: +49 (0)

More information

Mathematical Models with Maple

Mathematical Models with Maple Algebraic Biology 005 151 Mathematical Models with Maple Tetsu YAMAGUCHI Applied System nd Division, Cybernet Systems Co., Ltd., Otsuka -9-3, Bunkyo-ku, Tokyo 11-001, Japan tetsuy@cybernet.co.jp Abstract

More information

Estimation of Temperature Transients for Biomass Pretreatment in Tubular Batch Reactors and Impact on Xylan Hydrolysis Kinetics

Estimation of Temperature Transients for Biomass Pretreatment in Tubular Batch Reactors and Impact on Xylan Hydrolysis Kinetics Copyright Transients 2003 in Hydrolysis by Humana Press Kinetics Inc. 101 All rights of any nature whatsoever reserved. 0273-2289/03/105-108/0101/$20.00 Estimation of Temperature Transients for Biomass

More information

A First Course on Kinetics and Reaction Engineering Example 30.1

A First Course on Kinetics and Reaction Engineering Example 30.1 Example 30.1 Problem Purpose This problem will help you determine whether you have mastered the learning objectives for this unit. It illustrates the general approach to solving the design equations for

More information

Shortcut Distillation. Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia

Shortcut Distillation. Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia Shortcut Distillation Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia The use of separation column in HYSYS The column utilities in HYSYS can be used to model a wide variety of

More information

METHYL ACETATE REACTIVE DISTILLATION PROCESS MODELING, SIMULATION AND OPTIMIZATION USING ASPEN PLUS

METHYL ACETATE REACTIVE DISTILLATION PROCESS MODELING, SIMULATION AND OPTIMIZATION USING ASPEN PLUS METHYL ACETATE REACTIVE DISTILLATION PROCESS MODELING, SIMULATION AND OPTIMIZATION USING ASPEN PLUS Abdulwahab GIWA Department of Chemical Engineering, Faculty of Engineering, Middle East Technical University,

More information