Chemical Thermodynamics for Process SimulationISBN: 9783527312771
760 pages
March 2012

Description
This is the only book to apply thermodynamics to realworld process engineering problems, explaining the thermodynamics behind simulations from the view of academic and industrial authors to users of simulation programs. It comprises numerous solved examples, which simplify the understanding of the often complex calculation procedures, and discusses their advantages and disadvantages. The text also includes such special models as for formaldehyde, polymers, and associating compounds. Estimation methods for thermophysical properties and phase equilibria and thermodynamics of alternative separation processes are covered, as are new developments from recent years.
For a deeper understanding additional problems are given at the end of each chapter. To solve the complex problems prepared Mathcad files, Excel files or the DDBSP Explorer version can be accessed via the Internet.
While written for an advanced level, the text is easy to understand for every chemical engineer and chemist with a basic education in thermodynamics and phase equilibria, teaching students the engineering perspective of thermodynamics but also of interest to all companies active in chemistry, pharmacy, oil and gas processing, petrochemistry, refinery, food production, environmental protection and engineering.
For a deeper understanding additional problems are given at the end of each chapter. To solve the complex problems prepared Mathcad files, Excel files or the DDBSP Explorer version can be accessed via the Internet.
While written for an advanced level, the text is easy to understand for every chemical engineer and chemist with a basic education in thermodynamics and phase equilibria, teaching students the engineering perspective of thermodynamics but also of interest to all companies active in chemistry, pharmacy, oil and gas processing, petrochemistry, refinery, food production, environmental protection and engineering.
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Table of Contents
INTRODUCTION
PVT BEHAVIOR OF PURE COMPONENTS General Description Caloric Properties
Ideal Gases
Real Fluids
Equations of State
CORRELATION AND ESTIMATION OF PURE COMPONENT PROPERTIES
Characteristic Physical Property Constants
TemperatureDependent Properties
Correlation and Estimation of Transport Properties
PROPERTIES OF MIXTURES
Property Changes of Mixing
Partial Molar Properties
GibbsDuhem Equation
Ideal Mixture of Ideal Gases
Ideal Mixture of Real Fluids
Excess Properties
Fugacity in Mixtures
Activity and Activity Coefficient
Application of Equations of State to Mixtures
PHASE EQUILIBRIA IN FLUID SYSTEMS
Thermodynamic Fundamentals
Application of Activity Coefficient Models
Calculation of VaporLiquid Equilibria Using gEModels
Fitting of gEModel Parameters
Calculation of VaporLiquid Equilibria Using Equations of State
Conditions for the Occurrence of Azeotropic Behavior
Solubility of Gases in Liquids
LiquidLiquid Equilibria
Predictive Models
CALORIC PROPERTIES
Caloric Equations of State
Enthalpy Description in Process Simulation Programs
Caloric Properties in Chemical Reactions
The GMinimization Technique
ELECTROLYTE SOLUTIONS
Introduction
Thermodynamics of Electrolyte Solutions
Activity Coefficient Models for Electrolyte Solutions
Dissociation Equilibria
Influence of Salts on the VaporLiquid Equilibrium Behavior
Complex Electrolyte Systems
SOLIDLIQUID EQUILIBRIA
Thermodynamic Relations for the Calculation of SolidLiquid Equilibria
Salt Solubility
Solubility of Solids in Supercritical Fluids
MEMBRANE PROCESSES
Osmosis
Pervaporation
POLYMER THERMODYNAMICS
Introduction
gEmodels
Equations of State
Influence of Polydispersity
APPLICATIONS OF THERMODYNAMICS IN SEPARATION TECHNOLOGY
Verification of Model Parameters Prior to Process Simulation
Investigation of Azeotropic Points in Multicomponent Systems
Residue Curves, Distillation Boundaries, and Distillation Regions
Selection of Entrainers for Azeotropic and Extractive Distillation
Selection of Solvents for Other Separation Processes
Examination of the Applicability of Extractive Distillation for the Separation of Aliphatics from Aromatics
ENTHALPY OF REACTION AND CHEMICAL EQUILIBRIA
Enthalpy of Reaction
Chemical Equilibrium
Multiple Chemical Reaction Equilibria
SPECIAL APPLICATIONS
Formaldehyde Solutions
Vapor Phase Association
PRACTICAL APPLICATIONS
Flash
JouleThomson Effect
Adiabatic Compression and Expansion
Pressure Relief
Limitations of Equilibrium Thermodynamics
INTRODUCTION TO THE COLLECTION OF EXAMPLE PROBLEMS
Mathcad Examples
Examples Using the Dortmund Data Bank (DDB) and the Integrated Software Package DDBSP
Examples Using Microsoft Excel and Microsoft Office VBA
APPENDIX A Pure Component Parameters
APPENDIX B Coefficients for High Precision Equations of State
APPENDIX C Useful Derivations
APPENDIX D Standard Thermodynamic Properties for Selected Electrolyte Compounds
APPENDIX E Regression Technique for Pure Component Data
APPENDIX F Regression Techniques for Binary Parameters Appendix G Ideal Gas Heat Capacity Polynomial Coefficients for Selected Compounds
APPENDIX H UNIFAC Parameters
APPENDIX I Modified UNIFAC Parameters
APPENDIX J PSRK Parameters
APPENDIX K VTPR Parameters
Index
PVT BEHAVIOR OF PURE COMPONENTS General Description Caloric Properties
Ideal Gases
Real Fluids
Equations of State
CORRELATION AND ESTIMATION OF PURE COMPONENT PROPERTIES
Characteristic Physical Property Constants
TemperatureDependent Properties
Correlation and Estimation of Transport Properties
PROPERTIES OF MIXTURES
Property Changes of Mixing
Partial Molar Properties
GibbsDuhem Equation
Ideal Mixture of Ideal Gases
Ideal Mixture of Real Fluids
Excess Properties
Fugacity in Mixtures
Activity and Activity Coefficient
Application of Equations of State to Mixtures
PHASE EQUILIBRIA IN FLUID SYSTEMS
Thermodynamic Fundamentals
Application of Activity Coefficient Models
Calculation of VaporLiquid Equilibria Using gEModels
Fitting of gEModel Parameters
Calculation of VaporLiquid Equilibria Using Equations of State
Conditions for the Occurrence of Azeotropic Behavior
Solubility of Gases in Liquids
LiquidLiquid Equilibria
Predictive Models
CALORIC PROPERTIES
Caloric Equations of State
Enthalpy Description in Process Simulation Programs
Caloric Properties in Chemical Reactions
The GMinimization Technique
ELECTROLYTE SOLUTIONS
Introduction
Thermodynamics of Electrolyte Solutions
Activity Coefficient Models for Electrolyte Solutions
Dissociation Equilibria
Influence of Salts on the VaporLiquid Equilibrium Behavior
Complex Electrolyte Systems
SOLIDLIQUID EQUILIBRIA
Thermodynamic Relations for the Calculation of SolidLiquid Equilibria
Salt Solubility
Solubility of Solids in Supercritical Fluids
MEMBRANE PROCESSES
Osmosis
Pervaporation
POLYMER THERMODYNAMICS
Introduction
gEmodels
Equations of State
Influence of Polydispersity
APPLICATIONS OF THERMODYNAMICS IN SEPARATION TECHNOLOGY
Verification of Model Parameters Prior to Process Simulation
Investigation of Azeotropic Points in Multicomponent Systems
Residue Curves, Distillation Boundaries, and Distillation Regions
Selection of Entrainers for Azeotropic and Extractive Distillation
Selection of Solvents for Other Separation Processes
Examination of the Applicability of Extractive Distillation for the Separation of Aliphatics from Aromatics
ENTHALPY OF REACTION AND CHEMICAL EQUILIBRIA
Enthalpy of Reaction
Chemical Equilibrium
Multiple Chemical Reaction Equilibria
SPECIAL APPLICATIONS
Formaldehyde Solutions
Vapor Phase Association
PRACTICAL APPLICATIONS
Flash
JouleThomson Effect
Adiabatic Compression and Expansion
Pressure Relief
Limitations of Equilibrium Thermodynamics
INTRODUCTION TO THE COLLECTION OF EXAMPLE PROBLEMS
Mathcad Examples
Examples Using the Dortmund Data Bank (DDB) and the Integrated Software Package DDBSP
Examples Using Microsoft Excel and Microsoft Office VBA
APPENDIX A Pure Component Parameters
APPENDIX B Coefficients for High Precision Equations of State
APPENDIX C Useful Derivations
APPENDIX D Standard Thermodynamic Properties for Selected Electrolyte Compounds
APPENDIX E Regression Technique for Pure Component Data
APPENDIX F Regression Techniques for Binary Parameters Appendix G Ideal Gas Heat Capacity Polynomial Coefficients for Selected Compounds
APPENDIX H UNIFAC Parameters
APPENDIX I Modified UNIFAC Parameters
APPENDIX J PSRK Parameters
APPENDIX K VTPR Parameters
Index
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Author Information
Jürgen Gmehling studied chemical engineering in Essen and chemistry at the University of Dortmund, where he gained his doctorate in inorganic chemistry in 1973. From 19771978 he worked with Prof. J.M. Prausnitz at the Department of Chemical Engineering in Berkeley, California, before taking up his present post as Professor of Chemical Engineering at the University of Oldenburg in 1989. He is also president and CEO of DDBST GmbH, Oldenburg, as well as cofounder of LTP GmbH, part of the Carl von Ossietzky University of Oldenburg. Professor Gmehling has received various awards, such as the ArnoldEucken Prize from the GVC, the Rossini Lecture Award 2008 from the International Association of Chemical Thermodynamics, and the GmelinBeilstein Denkmünze from the GDCh. His research is concentrated on the computeraided synthesis, design and optimization of chemical processes.
After graduating in chemical engineering, Bärbel Kolbe completed her thesis in 1983 at the University of Dortmund in the research group led by Jürgen Gmehling, with whom she continued to work for another three years. During this time she participated in the publication of the Dechema Chemistry Data Series on VLE as well as the first edition of this book in German. Dr. Kolbe has been working for over twenty years as a senior process engineer first for Krupp Koppers GmbH and, since 1997, for ThyssenKrupp Uhde. The main focus of her research is on thermophysical properties, thermal separation technology and new processes.
After graduating in mechanical engineering, Michael Kleiber worked as a scientific assistant at the TU Brunswick, where he completed his thesis in 1994. After this, he worked for the former Hoechst AG and its successors in the fields of process development, process simulation and engineering calculations, before moving to ThyssenKrupp Uhde as a Chief Development Engineer. Dr. Kleiber is a member of the German Board of Thermodynamics and contributor to several standard works on process engineering, such as the VDI Heat Atlas, WinnackerKüchler and Ullmann's Encyclopedia of Industrial Chemistry.
Jürgen Rarey studied chemistry and gained his PhD in chemical engineering. He has held a permanent position at the University of Oldenburg in Prof. Gmehling's group since 1989, the same year he cofounded DDBST GmbH. For the past 20 years he has taught many courses on applied thermodynamics for chemical process simulation for external participants from industry both in Oldenburg, as well as inhouse for companies from around the world. Dr. Rarey is also an honorary professor in Durban, South Africa.
After graduating in chemical engineering, Bärbel Kolbe completed her thesis in 1983 at the University of Dortmund in the research group led by Jürgen Gmehling, with whom she continued to work for another three years. During this time she participated in the publication of the Dechema Chemistry Data Series on VLE as well as the first edition of this book in German. Dr. Kolbe has been working for over twenty years as a senior process engineer first for Krupp Koppers GmbH and, since 1997, for ThyssenKrupp Uhde. The main focus of her research is on thermophysical properties, thermal separation technology and new processes.
After graduating in mechanical engineering, Michael Kleiber worked as a scientific assistant at the TU Brunswick, where he completed his thesis in 1994. After this, he worked for the former Hoechst AG and its successors in the fields of process development, process simulation and engineering calculations, before moving to ThyssenKrupp Uhde as a Chief Development Engineer. Dr. Kleiber is a member of the German Board of Thermodynamics and contributor to several standard works on process engineering, such as the VDI Heat Atlas, WinnackerKüchler and Ullmann's Encyclopedia of Industrial Chemistry.
Jürgen Rarey studied chemistry and gained his PhD in chemical engineering. He has held a permanent position at the University of Oldenburg in Prof. Gmehling's group since 1989, the same year he cofounded DDBST GmbH. For the past 20 years he has taught many courses on applied thermodynamics for chemical process simulation for external participants from industry both in Oldenburg, as well as inhouse for companies from around the world. Dr. Rarey is also an honorary professor in Durban, South Africa.
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Reviews
"The authors of this excellent book on chemical thermodynamics have achieved something rare taking one of the dreariest theoretical sciences and making
it accessible.
This book is a treasure trove of fundamental thermodynamic knowledge with the guidance necessary to apply the theory to practical applications.
The first eight chapters deal primarily with thermodynamic concepts, such as pure component behaviour (Chapter 1). properties of mixtures (Chapter 2), phase equilibria and solid state equilibria (Chapters 4 and 8). In each of these chapters the authors manage to breakdown thermodynamics into its essential building blocks and guide the reader through the increasing complexity. This is a good refresher for those who studied thermodynamics as a student or a good introduction to those being exposed to thermodynamics for the first time.
However, be warned. This is not the basics of thermodynamics: the reader quickly gets amongst the mathematics  but it is present in a direct and concise manner that anyone familiar with undergraduate mathematics will be able to comprehend.
Though the title has 'for process simulations, most of the thermodynamic discussion is on the fundamental Level, with only the later parts of each chapter progressing into simulation models. Examples are equations of state for fluid system phase equilibria (Chapter1) and the NRTL model in electrolyte solutions (Chapter 7). This distinction makes Chemical thermodynamics for process simulations a great general reference
source.
The worked examples hit the Goldilocks zone for problems  not too easy, not too hard  and this reviewer found them to successfully illustrate the various topics.
The second half of the book focuses more on the applied side > applying thermodynamic theory to membrane processes (Chapter 9) and polymers (Chapter 10), as well as to reactions and equilibriums (Chapter 12). Here, the reader can become confused if not well versed in the topics of interest, since some prior knowledge is assumed.
The final chapter is not really a chapter, but rather an invitation for readers to download thermodynamic and process examples from the internet to be applied in software programs such as Mathcad. This is a great example of broadening the education value through technology, and should be copied bymore authors.
If you are interested in detailed and accessible thermodynamics, start and finish with this book."
 Chemistry in Australia, September 2012
it accessible.
This book is a treasure trove of fundamental thermodynamic knowledge with the guidance necessary to apply the theory to practical applications.
The first eight chapters deal primarily with thermodynamic concepts, such as pure component behaviour (Chapter 1). properties of mixtures (Chapter 2), phase equilibria and solid state equilibria (Chapters 4 and 8). In each of these chapters the authors manage to breakdown thermodynamics into its essential building blocks and guide the reader through the increasing complexity. This is a good refresher for those who studied thermodynamics as a student or a good introduction to those being exposed to thermodynamics for the first time.
However, be warned. This is not the basics of thermodynamics: the reader quickly gets amongst the mathematics  but it is present in a direct and concise manner that anyone familiar with undergraduate mathematics will be able to comprehend.
Though the title has 'for process simulations, most of the thermodynamic discussion is on the fundamental Level, with only the later parts of each chapter progressing into simulation models. Examples are equations of state for fluid system phase equilibria (Chapter1) and the NRTL model in electrolyte solutions (Chapter 7). This distinction makes Chemical thermodynamics for process simulations a great general reference
source.
The worked examples hit the Goldilocks zone for problems  not too easy, not too hard  and this reviewer found them to successfully illustrate the various topics.
The second half of the book focuses more on the applied side > applying thermodynamic theory to membrane processes (Chapter 9) and polymers (Chapter 10), as well as to reactions and equilibriums (Chapter 12). Here, the reader can become confused if not well versed in the topics of interest, since some prior knowledge is assumed.
The final chapter is not really a chapter, but rather an invitation for readers to download thermodynamic and process examples from the internet to be applied in software programs such as Mathcad. This is a great example of broadening the education value through technology, and should be copied bymore authors.
If you are interested in detailed and accessible thermodynamics, start and finish with this book."
 Chemistry in Australia, September 2012
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