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Microstructured devices for chemical processing / / Madhvanand N. Kashid, Albert Renken, and Lioubov Kiwi-Minsker
| Microstructured devices for chemical processing / / Madhvanand N. Kashid, Albert Renken, and Lioubov Kiwi-Minsker |
| Autore | Kashid Madhvanand N. |
| Pubbl/distr/stampa | Weinheim, Germany : , : Wiley-VCH, , 2014 |
| Descrizione fisica | 1 online resource (381 p.) |
| Disciplina | 660.28 |
| Soggetto topico | Chemical processes - Study and teaching |
| ISBN |
3-527-68518-9
3-527-68522-7 3-527-68519-7 |
| Formato | Materiale a stampa  |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
Microstructured Devices for Chemical Processing; Contents; Preface; List of Symbols; Chapter 1 Overview of Micro Reaction Engineering; 1.1 Introduction; 1.2 What are Microstructured Devices?; 1.3 Advantages of Microstructured Devices; 1.3.1 Enhancement of Transfer Rates; 1.3.2 Enhanced Process Safety; 1.3.3 Novel Operating Window; 1.3.4 Numbering-Up Instead of Scale-Up; 1.4 Materials and Methods for Fabrication of Microstructured Devices; 1.5 Applications of Microstructured Devices; 1.5.1 Microstructured Reactors as Research Tool; 1.5.2 Industrial/Commercial Applications
1.6 Structure of the Book1.7 Summary; References; Chapter 2 Basis of Chemical Reactor Design and Engineering; 2.1 Mass and Energy Balance; 2.2 Formal Kinetics of Homogenous Reactions; 2.2.1 Formal Kinetics of Single Homogenous Reactions; 2.2.2 Formal Kinetics of Multiple Homogenous Reactions; 2.2.3 Reaction Mechanism; 2.2.4 Homogenous Catalytic Reactions; 2.3 Ideal Reactors and Their Design Equations; 2.3.1 Performance Parameters; 2.3.2 Batch Wise-Operated Stirred Tank Reactor (BSTR); 2.3.3 Continuous Stirred Tank Reactor (CSTR); 2.3.4 Plug Flow or Ideal Tubular Reactor (PFR) 2.4 Homogenous Catalytic Reactions in Biphasic Systems2.5 Heterogenous Catalytic Reactions; 2.5.1 Rate Equations for Intrinsic Surface Reactions; 2.5.1.1 The Langmuir Adsorption Isotherms; 2.5.1.2 Basic Kinetic Models of Catalytic Heterogenous Reactions; 2.5.2 Deactivation of Heterogenous Catalysts; 2.6 Mass and Heat Transfer Effects on Heterogenous Catalytic Reactions; 2.6.1 External Mass and Heat Transfer; 2.6.1.1 Isothermal Pellet; 2.6.2 Internal Mass and Heat Transfer; 2.6.2.1 Isothermal Pellet; 2.6.2.2 Nonisothermal Pellet 2.6.2.3 Combination of External and Internal Transfer Resistances2.6.2.4 Internal and External Mass Transport in Isothermal Pellets; 2.6.2.5 The Temperature Dependence of the Effective Reaction Rate; 2.6.2.6 External and Internal Temperature Gradient; 2.6.3 Criteria for the Estimation of Transport Effects; 2.7 Summary; 2.8 List of Symbols; References; Chapter 3 Real Reactors and Residence Time Distribution (RTD); 3.1 Nonideal Flow Pattern and Definition of RTD; 3.2 Experimental Determination of RTD in Flow Reactors; 3.2.1 Step Function Stimulus-Response Method 3.2.2 Pulse Function Stimulus-Response Method3.3 RTD in Ideal Homogenous Reactors; 3.3.1 Ideal Plug Flow Reactor; 3.3.2 Ideal Continuously Operated Stirred Tank Reactor (CSTR); 3.3.3 Cascade of Ideal CSTR; 3.4 RTD in Nonideal Homogeneous Reactors; 3.4.1 Laminar Flow Tubular Reactors; 3.4.2 RTD Models for Real Reactors; 3.4.2.1 Tanks in Series Model; 3.4.2.2 Dispersion Model; 3.4.3 Estimation of RTD in Tubular Reactors; 3.5 Influence of RTD on the Reactor Performance; 3.5.1 Performance Estimation Based on Measured RTD; 3.5.2 Performance Estimation Based on RTD Models; 3.5.2.1 Dispersion Model 3.5.2.2 Tanks in Series Model |
| Record Nr. | UNINA-9910132188803321 |
Kashid Madhvanand N.
|
||
| Weinheim, Germany : , : Wiley-VCH, , 2014 | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||
Microstructured devices for chemical processing / / Madhvanand N. Kashid, Albert Renken, and Lioubov Kiwi-Minsker
| Microstructured devices for chemical processing / / Madhvanand N. Kashid, Albert Renken, and Lioubov Kiwi-Minsker |
| Autore | Kashid Madhvanand N. |
| Pubbl/distr/stampa | Weinheim, Germany : , : Wiley-VCH, , 2014 |
| Descrizione fisica | 1 online resource (381 p.) |
| Disciplina | 660.28 |
| Soggetto topico | Chemical processes - Study and teaching |
| ISBN |
3-527-68518-9
3-527-68522-7 3-527-68519-7 |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
Microstructured Devices for Chemical Processing; Contents; Preface; List of Symbols; Chapter 1 Overview of Micro Reaction Engineering; 1.1 Introduction; 1.2 What are Microstructured Devices?; 1.3 Advantages of Microstructured Devices; 1.3.1 Enhancement of Transfer Rates; 1.3.2 Enhanced Process Safety; 1.3.3 Novel Operating Window; 1.3.4 Numbering-Up Instead of Scale-Up; 1.4 Materials and Methods for Fabrication of Microstructured Devices; 1.5 Applications of Microstructured Devices; 1.5.1 Microstructured Reactors as Research Tool; 1.5.2 Industrial/Commercial Applications
1.6 Structure of the Book1.7 Summary; References; Chapter 2 Basis of Chemical Reactor Design and Engineering; 2.1 Mass and Energy Balance; 2.2 Formal Kinetics of Homogenous Reactions; 2.2.1 Formal Kinetics of Single Homogenous Reactions; 2.2.2 Formal Kinetics of Multiple Homogenous Reactions; 2.2.3 Reaction Mechanism; 2.2.4 Homogenous Catalytic Reactions; 2.3 Ideal Reactors and Their Design Equations; 2.3.1 Performance Parameters; 2.3.2 Batch Wise-Operated Stirred Tank Reactor (BSTR); 2.3.3 Continuous Stirred Tank Reactor (CSTR); 2.3.4 Plug Flow or Ideal Tubular Reactor (PFR) 2.4 Homogenous Catalytic Reactions in Biphasic Systems2.5 Heterogenous Catalytic Reactions; 2.5.1 Rate Equations for Intrinsic Surface Reactions; 2.5.1.1 The Langmuir Adsorption Isotherms; 2.5.1.2 Basic Kinetic Models of Catalytic Heterogenous Reactions; 2.5.2 Deactivation of Heterogenous Catalysts; 2.6 Mass and Heat Transfer Effects on Heterogenous Catalytic Reactions; 2.6.1 External Mass and Heat Transfer; 2.6.1.1 Isothermal Pellet; 2.6.2 Internal Mass and Heat Transfer; 2.6.2.1 Isothermal Pellet; 2.6.2.2 Nonisothermal Pellet 2.6.2.3 Combination of External and Internal Transfer Resistances2.6.2.4 Internal and External Mass Transport in Isothermal Pellets; 2.6.2.5 The Temperature Dependence of the Effective Reaction Rate; 2.6.2.6 External and Internal Temperature Gradient; 2.6.3 Criteria for the Estimation of Transport Effects; 2.7 Summary; 2.8 List of Symbols; References; Chapter 3 Real Reactors and Residence Time Distribution (RTD); 3.1 Nonideal Flow Pattern and Definition of RTD; 3.2 Experimental Determination of RTD in Flow Reactors; 3.2.1 Step Function Stimulus-Response Method 3.2.2 Pulse Function Stimulus-Response Method3.3 RTD in Ideal Homogenous Reactors; 3.3.1 Ideal Plug Flow Reactor; 3.3.2 Ideal Continuously Operated Stirred Tank Reactor (CSTR); 3.3.3 Cascade of Ideal CSTR; 3.4 RTD in Nonideal Homogeneous Reactors; 3.4.1 Laminar Flow Tubular Reactors; 3.4.2 RTD Models for Real Reactors; 3.4.2.1 Tanks in Series Model; 3.4.2.2 Dispersion Model; 3.4.3 Estimation of RTD in Tubular Reactors; 3.5 Influence of RTD on the Reactor Performance; 3.5.1 Performance Estimation Based on Measured RTD; 3.5.2 Performance Estimation Based on RTD Models; 3.5.2.1 Dispersion Model 3.5.2.2 Tanks in Series Model |
| Record Nr. | UNINA-9910824839803321 |
|
Kashid Madhvanand N.
|
||
| Weinheim, Germany : , : Wiley-VCH, , 2014 | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||