Attainable region theory : an introduction to choosing an optimal reactor / / by David Ming [and three others] |
Autore | Ming David <1985-> |
Pubbl/distr/stampa | Hoboken, New Jersey : , : Wiley, , 2016 |
Descrizione fisica | 1 online resource (370 p.) |
Disciplina | 660/.2832 |
Soggetto topico |
Chemical reactors - Design and construction
Statistical tolerance regions |
ISBN |
1-119-24470-6
1-119-24471-4 1-119-24469-2 |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Cover; Title Page; Copyright; Contents; Preface; Acknowledgments; Prior Knowledge; How this book is Structured; Software and Companion Website; Nomenclature; Section I Basic Theory; Chapter 1 Introduction; 1.1 Introduction; 1.2 Motivation; 1.3 Reactor Network Synthesis; 1.4 Solving the Reactor Network Synthesis Problem; 1.5 Chapter Review; References; Chapter 2 Concentration and Mixing; 2.1 Introduction; 2.2 Concentration Vectors and Dimension; 2.3 Mixing; 2.4 Chapter Review; References; Chapter 3 The Attainable Region; 3.1 Introduction; 3.2 A Mixing and Reaction Game; 3.3 The AR
3.4 Elementary Properties of the AR3.5 Chapter Review; References; Chapter 4 Reaction; 4.1 Introduction; 4.2 Reaction Rates and Stoichiometry; 4.3 Reaction from a Geometric Viewpoint; 4.4 Three Fundamental Continuous Reactor Types; 4.5 Summary; 4.6 Mixing Temperatures; 4.7 Additional Properties of the AR; 4.8 Chapter Review; References; Chapter 5 Two-Dimensional Constructions; 5.1 Introduction; 5.2 A Framework for Tackling AR Problems; 5.3 Two-Dimensional Van De Vusse Kinetics; 5.4 Multiple CSTR Steady States and ISOLAS; 5.5 Constructions in Residence Time Space; 5.6 Chapter Review ReferencesSection II Extended Topics; Chapter 6 Higher Dimensional AR Theory; 6.1 Introduction; 6.2 Dimension and Stoichiometry; 6.3 The Three Fundamental Reactor Types Used in AR Theory; 6.4 Critical DSR\textscs and CSTR\textscs; 6.5 Chapter Review; References; Chapter 7 Applications of AR Theory; 7.1 Introduction; 7.2 Higher Dimensional Constructions; 7.3 Nonisothermal Constructions and Reactor Type Constraints; 7.4 AR Theory for Batch Reactors; 7.5 Chapter Review; References; Chapter 8 AR Construction Algorithms; 8.1 Introduction; 8.2 Preliminaries; 8.3 Overview of AR Construction Methods 8.4 Inside-out Construction Methods8.5 Outside-in Construction Methods; 8.6 Superstructure Methods; 8.7 Chapter Review; References; Chapter 9 Attainable Regions for Variable Density Systems; 9.1 Introduction; 9.2 Common Conversions to Mass Fraction Space; 9.3 Examples; 9.4 Chapter Review; References; Chapter 10 Final Remarks, Further Reading, and Future Directions; 10.1 Introduction; 10.2 Chapter Summaries and Final Remarks; 10.3 Further Reading; 10.4 Future Directions; References; Appendix A Fundamental Reactor Types; A.1 The Plug Flow Reactor; A.2 The Continuous-Flow Stirred Tank Reactor A.3 The Differential Sidestream ReactorAppendix B Mathematical Topics; B.1 Set Notation; B.2 Aspects of Linear Algebra; B.3 The Complement Principle; References; Appendix C Companion Software and Website; C.1 Introduction; C.2 Obtaining Python and Jupyter; Index; Supplemental Images; EULA |
Record Nr. | UNINA-9910135031003321 |
Ming David <1985->
![]() |
||
Hoboken, New Jersey : , : Wiley, , 2016 | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Attainable region theory : an introduction to choosing an optimal reactor / / by David Ming [and three others] |
Autore | Ming David <1985-> |
Pubbl/distr/stampa | Hoboken, New Jersey : , : Wiley, , 2016 |
Descrizione fisica | 1 online resource (370 p.) |
Disciplina | 660/.2832 |
Soggetto topico |
Chemical reactors - Design and construction
Statistical tolerance regions |
ISBN |
1-119-24470-6
1-119-24471-4 1-119-24469-2 |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
Cover; Title Page; Copyright; Contents; Preface; Acknowledgments; Prior Knowledge; How this book is Structured; Software and Companion Website; Nomenclature; Section I Basic Theory; Chapter 1 Introduction; 1.1 Introduction; 1.2 Motivation; 1.3 Reactor Network Synthesis; 1.4 Solving the Reactor Network Synthesis Problem; 1.5 Chapter Review; References; Chapter 2 Concentration and Mixing; 2.1 Introduction; 2.2 Concentration Vectors and Dimension; 2.3 Mixing; 2.4 Chapter Review; References; Chapter 3 The Attainable Region; 3.1 Introduction; 3.2 A Mixing and Reaction Game; 3.3 The AR
3.4 Elementary Properties of the AR3.5 Chapter Review; References; Chapter 4 Reaction; 4.1 Introduction; 4.2 Reaction Rates and Stoichiometry; 4.3 Reaction from a Geometric Viewpoint; 4.4 Three Fundamental Continuous Reactor Types; 4.5 Summary; 4.6 Mixing Temperatures; 4.7 Additional Properties of the AR; 4.8 Chapter Review; References; Chapter 5 Two-Dimensional Constructions; 5.1 Introduction; 5.2 A Framework for Tackling AR Problems; 5.3 Two-Dimensional Van De Vusse Kinetics; 5.4 Multiple CSTR Steady States and ISOLAS; 5.5 Constructions in Residence Time Space; 5.6 Chapter Review ReferencesSection II Extended Topics; Chapter 6 Higher Dimensional AR Theory; 6.1 Introduction; 6.2 Dimension and Stoichiometry; 6.3 The Three Fundamental Reactor Types Used in AR Theory; 6.4 Critical DSR\textscs and CSTR\textscs; 6.5 Chapter Review; References; Chapter 7 Applications of AR Theory; 7.1 Introduction; 7.2 Higher Dimensional Constructions; 7.3 Nonisothermal Constructions and Reactor Type Constraints; 7.4 AR Theory for Batch Reactors; 7.5 Chapter Review; References; Chapter 8 AR Construction Algorithms; 8.1 Introduction; 8.2 Preliminaries; 8.3 Overview of AR Construction Methods 8.4 Inside-out Construction Methods8.5 Outside-in Construction Methods; 8.6 Superstructure Methods; 8.7 Chapter Review; References; Chapter 9 Attainable Regions for Variable Density Systems; 9.1 Introduction; 9.2 Common Conversions to Mass Fraction Space; 9.3 Examples; 9.4 Chapter Review; References; Chapter 10 Final Remarks, Further Reading, and Future Directions; 10.1 Introduction; 10.2 Chapter Summaries and Final Remarks; 10.3 Further Reading; 10.4 Future Directions; References; Appendix A Fundamental Reactor Types; A.1 The Plug Flow Reactor; A.2 The Continuous-Flow Stirred Tank Reactor A.3 The Differential Sidestream ReactorAppendix B Mathematical Topics; B.1 Set Notation; B.2 Aspects of Linear Algebra; B.3 The Complement Principle; References; Appendix C Companion Software and Website; C.1 Introduction; C.2 Obtaining Python and Jupyter; Index; Supplemental Images; EULA |
Record Nr. | UNINA-9910807945003321 |
Ming David <1985->
![]() |
||
Hoboken, New Jersey : , : Wiley, , 2016 | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemical reactor design : mathematical modeling and applications / / Juan A. Conesa |
Autore | Conesa Juan A. |
Pubbl/distr/stampa | Weinheim, Germany : , : Wiley-VCH, , [2020] |
Descrizione fisica | 1 online resource (353 pages) |
Disciplina | 660.2832 |
Soggetto topico | Chemical reactors - Design and construction |
Soggetto genere / forma | Electronic books. |
ISBN |
3-527-82338-7
1-5231-3284-1 3-527-82337-9 3-527-82339-5 |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Record Nr. | UNINA-9910555086503321 |
Conesa Juan A.
![]() |
||
Weinheim, Germany : , : Wiley-VCH, , [2020] | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemical reactor design : mathematical modeling and applications / / Juan A. Conesa |
Autore | Conesa Juan A. |
Pubbl/distr/stampa | Weinheim, Germany : , : Wiley-VCH, , [2020] |
Descrizione fisica | 1 online resource (353 pages) |
Disciplina | 660.2832 |
Soggetto topico | Chemical reactors - Design and construction |
ISBN |
3-527-82338-7
1-5231-3284-1 3-527-82337-9 3-527-82339-5 |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Record Nr. | UNINA-9910831026403321 |
Conesa Juan A.
![]() |
||
Weinheim, Germany : , : Wiley-VCH, , [2020] | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemical reactor design and control [[electronic resource] /] / William L. Luyben |
Autore | Luyben William L |
Pubbl/distr/stampa | [New York], : AIChE |
Descrizione fisica | 1 online resource (437 p.) |
Disciplina |
660.2832
660/.2832 |
Soggetto topico |
Chemical reactors - Design and construction
Reactors químics |
Soggetto genere / forma | Llibres electrònics |
ISBN |
1-281-00186-4
9786611001865 0-470-13491-7 0-470-13490-9 |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
CHEMICAL REACTOR DESIGN AND CONTROL; CONTENTS; PREFACE; 1 REACTOR BASICS; 1.1 Fundamentals of Kinetics and Reaction Equilibrium; 1.1.1 Power-Law Kinetics; 1.1.2 Heterogeneous Reaction Kinetics; 1.1.3 Biochemical Reaction Kinetics; 1.1.4 Literature; 1.2 Multiple Reactions; 1.2.1 Parallel Reactions; 1.2.2 Series Reactions; 1.3 Determining Kinetic Parameters; 1.4 Types and Fundamental Properties of Reactors; 1.4.1 Continuous Stirred-Tank Reactor; 1.4.2 Batch Reactor; 1.4.3 Tubular Plug Flow Reactor; 1.5 Heat Transfer in Reactors; 1.6 Reactor ScaleUp; 1.7 Conclusion
2.8.1 Simulation Setup2.8.2 Specifying Reactions; 2.8.3 Reactor Setup; 2.9 Optimization of CSTR Systems; 2.9.1 Economics of Series CSTRs; 2.9.2 Economics of a Reactor-Column Process; 2.9.3 CSTR Processes with Two Reactants; 2.10 Conclusion; 3 CONTROL OF CSTR SYSTEMS; 3.1 Irreversible, Single Reactant; 3.1.1 Nonlinear Dynamic Model; 3.1.2 Linear Model; 3.1.3 Effect of Conversion on Openloop and Closedloop Stability; 3.1.4 Nonlinear Dynamic Simulation; 3.1.5 Effect of Jacket Volume; 3.1.6 Cooling Coil; 3.1.7 External Heat Exchanger; 3.1.8 Comparison of CSTR-in-Series Processes 3.1.9 Dynamics of Reactor-Stripper Process3.2 Reactor-Column Process with Two Reactants; 3.2.1 Nonlinear Dynamic Model of Reactor and Column; 3.2.2 Control Structure for Reactor-Column Process; 3.2.3 Reactor-Column Process with Hot Reaction; 3.3 AutoRefrigerated Reactor Control; 3.3.1 Dynamic Model; 3.3.2 Simulation Results; 3.4 Reactor Temperature Control Using Feed Manipulation; 3.4.1 Introduction; 3.4.2 Revised Control Structure; 3.4.3 Results; 3.4.4 Valve Position Control; 3.5 Aspen Dynamics Simulation of CSTRs; 3.5.1 Setting up the Dynamic Simulation 3.5.2 Running the Simulation and Tuning Controllers3.5.3 Results with Several Heat Transfer Options; 3.5.4 Use of RGIBBS Reactor; 3.6 Conclusion; 4 CONTROL OF BATCH REACTORS; 4.1 Irreversible, Single Reactant; 4.1.1 Pure Batch Reactor; 4.1.2 Fed-Batch Reactor; 4.2 Batch Reactor with Two Reactants; 4.3 Batch Reactor with Consecutive Reactions; 4.4 Aspen Plus Simulation Using RBatch; 4.5 Ethanol Batch Fermentor; 4.6 Fed-Batch Hydrogenation Reactor; 4.7 Batch TML Reactor; 4.8 Fed-Batch Reactor with Multiple Reactions; 4.8.1 Equations; 4.8.2 Effect of Feed Trajectory on Conversion and Selectivity 4.8.3 Batch Optimization |
Record Nr. | UNINA-9910144003703321 |
Luyben William L
![]() |
||
[New York], : AIChE | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemical reactor design and control [[electronic resource] /] / William L. Luyben |
Autore | Luyben William L |
Pubbl/distr/stampa | [New York], : AIChE |
Descrizione fisica | 1 online resource (437 p.) |
Disciplina |
660.2832
660/.2832 |
Soggetto topico |
Chemical reactors - Design and construction
Reactors químics |
Soggetto genere / forma | Llibres electrònics |
ISBN |
1-281-00186-4
9786611001865 0-470-13491-7 0-470-13490-9 |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
CHEMICAL REACTOR DESIGN AND CONTROL; CONTENTS; PREFACE; 1 REACTOR BASICS; 1.1 Fundamentals of Kinetics and Reaction Equilibrium; 1.1.1 Power-Law Kinetics; 1.1.2 Heterogeneous Reaction Kinetics; 1.1.3 Biochemical Reaction Kinetics; 1.1.4 Literature; 1.2 Multiple Reactions; 1.2.1 Parallel Reactions; 1.2.2 Series Reactions; 1.3 Determining Kinetic Parameters; 1.4 Types and Fundamental Properties of Reactors; 1.4.1 Continuous Stirred-Tank Reactor; 1.4.2 Batch Reactor; 1.4.3 Tubular Plug Flow Reactor; 1.5 Heat Transfer in Reactors; 1.6 Reactor ScaleUp; 1.7 Conclusion
2.8.1 Simulation Setup2.8.2 Specifying Reactions; 2.8.3 Reactor Setup; 2.9 Optimization of CSTR Systems; 2.9.1 Economics of Series CSTRs; 2.9.2 Economics of a Reactor-Column Process; 2.9.3 CSTR Processes with Two Reactants; 2.10 Conclusion; 3 CONTROL OF CSTR SYSTEMS; 3.1 Irreversible, Single Reactant; 3.1.1 Nonlinear Dynamic Model; 3.1.2 Linear Model; 3.1.3 Effect of Conversion on Openloop and Closedloop Stability; 3.1.4 Nonlinear Dynamic Simulation; 3.1.5 Effect of Jacket Volume; 3.1.6 Cooling Coil; 3.1.7 External Heat Exchanger; 3.1.8 Comparison of CSTR-in-Series Processes 3.1.9 Dynamics of Reactor-Stripper Process3.2 Reactor-Column Process with Two Reactants; 3.2.1 Nonlinear Dynamic Model of Reactor and Column; 3.2.2 Control Structure for Reactor-Column Process; 3.2.3 Reactor-Column Process with Hot Reaction; 3.3 AutoRefrigerated Reactor Control; 3.3.1 Dynamic Model; 3.3.2 Simulation Results; 3.4 Reactor Temperature Control Using Feed Manipulation; 3.4.1 Introduction; 3.4.2 Revised Control Structure; 3.4.3 Results; 3.4.4 Valve Position Control; 3.5 Aspen Dynamics Simulation of CSTRs; 3.5.1 Setting up the Dynamic Simulation 3.5.2 Running the Simulation and Tuning Controllers3.5.3 Results with Several Heat Transfer Options; 3.5.4 Use of RGIBBS Reactor; 3.6 Conclusion; 4 CONTROL OF BATCH REACTORS; 4.1 Irreversible, Single Reactant; 4.1.1 Pure Batch Reactor; 4.1.2 Fed-Batch Reactor; 4.2 Batch Reactor with Two Reactants; 4.3 Batch Reactor with Consecutive Reactions; 4.4 Aspen Plus Simulation Using RBatch; 4.5 Ethanol Batch Fermentor; 4.6 Fed-Batch Hydrogenation Reactor; 4.7 Batch TML Reactor; 4.8 Fed-Batch Reactor with Multiple Reactions; 4.8.1 Equations; 4.8.2 Effect of Feed Trajectory on Conversion and Selectivity 4.8.3 Batch Optimization |
Record Nr. | UNINA-9910830065603321 |
Luyben William L
![]() |
||
[New York], : AIChE | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemical reactor design and control / / William L. Luyben |
Autore | Luyben William L |
Pubbl/distr/stampa | [New York], : AIChE |
Descrizione fisica | 1 online resource (437 p.) |
Disciplina | 660/.2832 |
Soggetto topico |
Chemical reactors - Design and construction
Reactors químics |
Soggetto genere / forma | Llibres electrònics |
ISBN |
1-281-00186-4
9786611001865 0-470-13491-7 0-470-13490-9 |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | eng |
Nota di contenuto |
CHEMICAL REACTOR DESIGN AND CONTROL; CONTENTS; PREFACE; 1 REACTOR BASICS; 1.1 Fundamentals of Kinetics and Reaction Equilibrium; 1.1.1 Power-Law Kinetics; 1.1.2 Heterogeneous Reaction Kinetics; 1.1.3 Biochemical Reaction Kinetics; 1.1.4 Literature; 1.2 Multiple Reactions; 1.2.1 Parallel Reactions; 1.2.2 Series Reactions; 1.3 Determining Kinetic Parameters; 1.4 Types and Fundamental Properties of Reactors; 1.4.1 Continuous Stirred-Tank Reactor; 1.4.2 Batch Reactor; 1.4.3 Tubular Plug Flow Reactor; 1.5 Heat Transfer in Reactors; 1.6 Reactor ScaleUp; 1.7 Conclusion
2.8.1 Simulation Setup2.8.2 Specifying Reactions; 2.8.3 Reactor Setup; 2.9 Optimization of CSTR Systems; 2.9.1 Economics of Series CSTRs; 2.9.2 Economics of a Reactor-Column Process; 2.9.3 CSTR Processes with Two Reactants; 2.10 Conclusion; 3 CONTROL OF CSTR SYSTEMS; 3.1 Irreversible, Single Reactant; 3.1.1 Nonlinear Dynamic Model; 3.1.2 Linear Model; 3.1.3 Effect of Conversion on Openloop and Closedloop Stability; 3.1.4 Nonlinear Dynamic Simulation; 3.1.5 Effect of Jacket Volume; 3.1.6 Cooling Coil; 3.1.7 External Heat Exchanger; 3.1.8 Comparison of CSTR-in-Series Processes 3.1.9 Dynamics of Reactor-Stripper Process3.2 Reactor-Column Process with Two Reactants; 3.2.1 Nonlinear Dynamic Model of Reactor and Column; 3.2.2 Control Structure for Reactor-Column Process; 3.2.3 Reactor-Column Process with Hot Reaction; 3.3 AutoRefrigerated Reactor Control; 3.3.1 Dynamic Model; 3.3.2 Simulation Results; 3.4 Reactor Temperature Control Using Feed Manipulation; 3.4.1 Introduction; 3.4.2 Revised Control Structure; 3.4.3 Results; 3.4.4 Valve Position Control; 3.5 Aspen Dynamics Simulation of CSTRs; 3.5.1 Setting up the Dynamic Simulation 3.5.2 Running the Simulation and Tuning Controllers3.5.3 Results with Several Heat Transfer Options; 3.5.4 Use of RGIBBS Reactor; 3.6 Conclusion; 4 CONTROL OF BATCH REACTORS; 4.1 Irreversible, Single Reactant; 4.1.1 Pure Batch Reactor; 4.1.2 Fed-Batch Reactor; 4.2 Batch Reactor with Two Reactants; 4.3 Batch Reactor with Consecutive Reactions; 4.4 Aspen Plus Simulation Using RBatch; 4.5 Ethanol Batch Fermentor; 4.6 Fed-Batch Hydrogenation Reactor; 4.7 Batch TML Reactor; 4.8 Fed-Batch Reactor with Multiple Reactions; 4.8.1 Equations; 4.8.2 Effect of Feed Trajectory on Conversion and Selectivity 4.8.3 Batch Optimization |
Record Nr. | UNINA-9910876592903321 |
Luyben William L
![]() |
||
[New York], : AIChE | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemiereaktoren [[electronic resource] ] : Auslegung und Simulation / / Jens Hagen |
Autore | Hagen Jens |
Pubbl/distr/stampa | Weinheim [Germany], : Wiley-VCH, 2004 |
Descrizione fisica | 1 online resource (400 p.) |
Disciplina |
660.068 / 5
660.0685 |
Soggetto topico |
Chemical reactors
Chemical reactors - Design and construction |
Soggetto genere / forma | Electronic books. |
ISBN |
3-527-66060-7
1-280-55785-0 9786610557851 3-527-66100-X 3-527-60359-X |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | ger |
Nota di contenuto |
Title Page; Inhaltsverzeichnis; Vorwort; Formelzeichen und Abkuumalrzungen; 1 Einfuumalhrung; 1.1 Die Aufgaben der Chemischen Reaktionstechnik; 1.2 Wirtschaftliche Prozessfuumalhrung; 2 Chemiereaktoren im Uumalberblick; 2.1 Betriebsweise und Grundtypen von Chemiereaktoren; 2.2 Beurteilungsgroumalben fuumalr Chemiereaktoren; 3 Physikalisch-chemische Aspekte der Reaktionstechnik; 3.1 Umsatz und Stoumalchiometrie; 3.2 Das chemische Gleichgewicht; 3.3 Reaktionskinetische Gleichungen; 3.4 Aufstellen der Materialbilanz; 3.5 Aufstellen der Waumalrmebilanz
4 Grundlagen der Reaktormodellierung und -simulation4.1 Mathematische Modelle; 4.2 Simulation; 5 Ideale, isotherm betriebene Reaktoren; 5.1 Der diskontinuierlich betriebene Ruumalhrkessel; 5.2 Der kontinuierlich betriebene Ruumalhrkessel; 5.3 Das Stroumalmungsrohr; 5.4 Reaktoren mit Kreislauffuumalhrung; 5.4.1 Der Kreislauf- oder Schlaufenreaktor; 5.4.2 Reaktor mit Trennstufe und Ruumalckfuumalhrung; 5.5 Halbkontinuierlich betriebene Reaktoren; 5.6 Reaktorkombinationen; 5.6.1 Die Ruumalhrkesselkaskade; 5.6.2 Reihenschaltung von Ruumalhrkessel und Stroumalmungsrohr 5.6.3 Reihen- und Parallelschaltung von Stroumalmungsrohren5.7 Leistungsvergleich der Idealreaktoren; 6 Messung und Auswertung kinetischer Daten fuumalr den Reaktorbetrieb; 6.1 Ruumalckvermischungseffekt bei einfachen Reaktionen; 6.2 Reaktordesign fuumalr komplexe Reaktionen; 6.2.1 Parallelreaktionen; 6.2.2 Folgereaktionen; 6.2.3 Komplexe Serienreaktionen; 6.2.4 Vergleichende Betrachtung von komplexen Reaktionen; 6.3 Laborreaktoren fuumalr kinetische Untersuchungen; 6.4 Analyse kinetischer Daten mittels Regression; 7 Nichtideale Reaktoren und Reaktormodelle; 7.1 Verweilzeitspektrum 7.2 Verweilzeitsummenfunktion und mittlere Verweilzeit7.3 Experimentelle Ermittlung der Verweilzeitkurven; 7.4 Verweilzeitverteilung und Umsatz in Realreaktoren; 7.5 Modellbetrachtungen; 7.5.1 Diffusions- und Kaskadenmodell; 7.5.2 Zwei-Parameter-Modell: Ruumalhrreaktor mit Totzone undKurzschluss-Stroumalmung; 7.5.3 Ruumalhrreaktor mit Kurzschluss-Stroumalmung und schlechtdurchmischter Zone; 7.6 Einfluss der Vermischung auf den Umsatz; 7.6.1 Segregation; 7.6.2 Zeitpunkt der Vermischung; 8 Reaktorauslegung unter Ber cksichtigung des Waumalrmetransports 8.1 Lenkung des Temperaturverlaufs in Reaktoren8.2 Waumalrmeumsatz in Reaktoren; 8.3 Waumalrmetechnische Auslegung von Chemiereaktoren; 8.3.1 Der diskontinuierlich betriebene Ruumalhrkessel; 8.3.2 Das ideale Stroumalmungsrohr; 8.3.3 Der kontinuierlich betriebene Ruumalhrkessel; 9 Der Einfluss des Stoffuumalbergangs auf den Reaktorbetrieb; 9.1 Fluid-Fluid-Reaktionen; 9.2 Heterogen katalysierte Reaktionen; 9.3 Druckverlust in Festbettreaktoren; 9.4 Reaktionen zwischen Gas, Fluumalssigkeit und Feststoff; 10 Technische Reaktionsfuumalhrung; 10.1 Auswahlkriterien fuumalr Chemiereaktoren 10.2 Reaktoren fuumalr homogene Reaktionen |
Record Nr. | UNINA-9910143964603321 |
Hagen Jens
![]() |
||
Weinheim [Germany], : Wiley-VCH, 2004 | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemiereaktoren [[electronic resource] ] : Auslegung und Simulation / / Jens Hagen |
Autore | Hagen Jens |
Pubbl/distr/stampa | Weinheim [Germany], : Wiley-VCH, 2004 |
Descrizione fisica | 1 online resource (400 p.) |
Disciplina |
660.068 / 5
660.0685 |
Soggetto topico |
Chemical reactors
Chemical reactors - Design and construction |
ISBN |
3-527-66060-7
1-280-55785-0 9786610557851 3-527-66100-X 3-527-60359-X |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | ger |
Nota di contenuto |
Title Page; Inhaltsverzeichnis; Vorwort; Formelzeichen und Abkuumalrzungen; 1 Einfuumalhrung; 1.1 Die Aufgaben der Chemischen Reaktionstechnik; 1.2 Wirtschaftliche Prozessfuumalhrung; 2 Chemiereaktoren im Uumalberblick; 2.1 Betriebsweise und Grundtypen von Chemiereaktoren; 2.2 Beurteilungsgroumalben fuumalr Chemiereaktoren; 3 Physikalisch-chemische Aspekte der Reaktionstechnik; 3.1 Umsatz und Stoumalchiometrie; 3.2 Das chemische Gleichgewicht; 3.3 Reaktionskinetische Gleichungen; 3.4 Aufstellen der Materialbilanz; 3.5 Aufstellen der Waumalrmebilanz
4 Grundlagen der Reaktormodellierung und -simulation4.1 Mathematische Modelle; 4.2 Simulation; 5 Ideale, isotherm betriebene Reaktoren; 5.1 Der diskontinuierlich betriebene Ruumalhrkessel; 5.2 Der kontinuierlich betriebene Ruumalhrkessel; 5.3 Das Stroumalmungsrohr; 5.4 Reaktoren mit Kreislauffuumalhrung; 5.4.1 Der Kreislauf- oder Schlaufenreaktor; 5.4.2 Reaktor mit Trennstufe und Ruumalckfuumalhrung; 5.5 Halbkontinuierlich betriebene Reaktoren; 5.6 Reaktorkombinationen; 5.6.1 Die Ruumalhrkesselkaskade; 5.6.2 Reihenschaltung von Ruumalhrkessel und Stroumalmungsrohr 5.6.3 Reihen- und Parallelschaltung von Stroumalmungsrohren5.7 Leistungsvergleich der Idealreaktoren; 6 Messung und Auswertung kinetischer Daten fuumalr den Reaktorbetrieb; 6.1 Ruumalckvermischungseffekt bei einfachen Reaktionen; 6.2 Reaktordesign fuumalr komplexe Reaktionen; 6.2.1 Parallelreaktionen; 6.2.2 Folgereaktionen; 6.2.3 Komplexe Serienreaktionen; 6.2.4 Vergleichende Betrachtung von komplexen Reaktionen; 6.3 Laborreaktoren fuumalr kinetische Untersuchungen; 6.4 Analyse kinetischer Daten mittels Regression; 7 Nichtideale Reaktoren und Reaktormodelle; 7.1 Verweilzeitspektrum 7.2 Verweilzeitsummenfunktion und mittlere Verweilzeit7.3 Experimentelle Ermittlung der Verweilzeitkurven; 7.4 Verweilzeitverteilung und Umsatz in Realreaktoren; 7.5 Modellbetrachtungen; 7.5.1 Diffusions- und Kaskadenmodell; 7.5.2 Zwei-Parameter-Modell: Ruumalhrreaktor mit Totzone undKurzschluss-Stroumalmung; 7.5.3 Ruumalhrreaktor mit Kurzschluss-Stroumalmung und schlechtdurchmischter Zone; 7.6 Einfluss der Vermischung auf den Umsatz; 7.6.1 Segregation; 7.6.2 Zeitpunkt der Vermischung; 8 Reaktorauslegung unter Ber cksichtigung des Waumalrmetransports 8.1 Lenkung des Temperaturverlaufs in Reaktoren8.2 Waumalrmeumsatz in Reaktoren; 8.3 Waumalrmetechnische Auslegung von Chemiereaktoren; 8.3.1 Der diskontinuierlich betriebene Ruumalhrkessel; 8.3.2 Das ideale Stroumalmungsrohr; 8.3.3 Der kontinuierlich betriebene Ruumalhrkessel; 9 Der Einfluss des Stoffuumalbergangs auf den Reaktorbetrieb; 9.1 Fluid-Fluid-Reaktionen; 9.2 Heterogen katalysierte Reaktionen; 9.3 Druckverlust in Festbettreaktoren; 9.4 Reaktionen zwischen Gas, Fluumalssigkeit und Feststoff; 10 Technische Reaktionsfuumalhrung; 10.1 Auswahlkriterien fuumalr Chemiereaktoren 10.2 Reaktoren fuumalr homogene Reaktionen |
Record Nr. | UNINA-9910830318803321 |
Hagen Jens
![]() |
||
Weinheim [Germany], : Wiley-VCH, 2004 | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|
Chemiereaktoren : Auslegung und Simulation / / Jens Hagen |
Autore | Hagen Jens |
Pubbl/distr/stampa | Weinheim [Germany], : Wiley-VCH, 2004 |
Descrizione fisica | 1 online resource (400 p.) |
Disciplina |
660.068 / 5
660.0685 |
Soggetto topico |
Chemical reactors
Chemical reactors - Design and construction |
ISBN |
3-527-66060-7
1-280-55785-0 9786610557851 3-527-66100-X 3-527-60359-X |
Formato | Materiale a stampa ![]() |
Livello bibliografico | Monografia |
Lingua di pubblicazione | ger |
Nota di contenuto |
Title Page; Inhaltsverzeichnis; Vorwort; Formelzeichen und Abkuumalrzungen; 1 Einfuumalhrung; 1.1 Die Aufgaben der Chemischen Reaktionstechnik; 1.2 Wirtschaftliche Prozessfuumalhrung; 2 Chemiereaktoren im Uumalberblick; 2.1 Betriebsweise und Grundtypen von Chemiereaktoren; 2.2 Beurteilungsgroumalben fuumalr Chemiereaktoren; 3 Physikalisch-chemische Aspekte der Reaktionstechnik; 3.1 Umsatz und Stoumalchiometrie; 3.2 Das chemische Gleichgewicht; 3.3 Reaktionskinetische Gleichungen; 3.4 Aufstellen der Materialbilanz; 3.5 Aufstellen der Waumalrmebilanz
4 Grundlagen der Reaktormodellierung und -simulation4.1 Mathematische Modelle; 4.2 Simulation; 5 Ideale, isotherm betriebene Reaktoren; 5.1 Der diskontinuierlich betriebene Ruumalhrkessel; 5.2 Der kontinuierlich betriebene Ruumalhrkessel; 5.3 Das Stroumalmungsrohr; 5.4 Reaktoren mit Kreislauffuumalhrung; 5.4.1 Der Kreislauf- oder Schlaufenreaktor; 5.4.2 Reaktor mit Trennstufe und Ruumalckfuumalhrung; 5.5 Halbkontinuierlich betriebene Reaktoren; 5.6 Reaktorkombinationen; 5.6.1 Die Ruumalhrkesselkaskade; 5.6.2 Reihenschaltung von Ruumalhrkessel und Stroumalmungsrohr 5.6.3 Reihen- und Parallelschaltung von Stroumalmungsrohren5.7 Leistungsvergleich der Idealreaktoren; 6 Messung und Auswertung kinetischer Daten fuumalr den Reaktorbetrieb; 6.1 Ruumalckvermischungseffekt bei einfachen Reaktionen; 6.2 Reaktordesign fuumalr komplexe Reaktionen; 6.2.1 Parallelreaktionen; 6.2.2 Folgereaktionen; 6.2.3 Komplexe Serienreaktionen; 6.2.4 Vergleichende Betrachtung von komplexen Reaktionen; 6.3 Laborreaktoren fuumalr kinetische Untersuchungen; 6.4 Analyse kinetischer Daten mittels Regression; 7 Nichtideale Reaktoren und Reaktormodelle; 7.1 Verweilzeitspektrum 7.2 Verweilzeitsummenfunktion und mittlere Verweilzeit7.3 Experimentelle Ermittlung der Verweilzeitkurven; 7.4 Verweilzeitverteilung und Umsatz in Realreaktoren; 7.5 Modellbetrachtungen; 7.5.1 Diffusions- und Kaskadenmodell; 7.5.2 Zwei-Parameter-Modell: Ruumalhrreaktor mit Totzone undKurzschluss-Stroumalmung; 7.5.3 Ruumalhrreaktor mit Kurzschluss-Stroumalmung und schlechtdurchmischter Zone; 7.6 Einfluss der Vermischung auf den Umsatz; 7.6.1 Segregation; 7.6.2 Zeitpunkt der Vermischung; 8 Reaktorauslegung unter Ber cksichtigung des Waumalrmetransports 8.1 Lenkung des Temperaturverlaufs in Reaktoren8.2 Waumalrmeumsatz in Reaktoren; 8.3 Waumalrmetechnische Auslegung von Chemiereaktoren; 8.3.1 Der diskontinuierlich betriebene Ruumalhrkessel; 8.3.2 Das ideale Stroumalmungsrohr; 8.3.3 Der kontinuierlich betriebene Ruumalhrkessel; 9 Der Einfluss des Stoffuumalbergangs auf den Reaktorbetrieb; 9.1 Fluid-Fluid-Reaktionen; 9.2 Heterogen katalysierte Reaktionen; 9.3 Druckverlust in Festbettreaktoren; 9.4 Reaktionen zwischen Gas, Fluumalssigkeit und Feststoff; 10 Technische Reaktionsfuumalhrung; 10.1 Auswahlkriterien fuumalr Chemiereaktoren 10.2 Reaktoren fuumalr homogene Reaktionen |
Record Nr. | UNINA-9910876934303321 |
Hagen Jens
![]() |
||
Weinheim [Germany], : Wiley-VCH, 2004 | ||
![]() | ||
Lo trovi qui: Univ. Federico II | ||
|