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Chemical Engineering Dynamics [[electronic resource] ] : Modelling with PC Simulation
| Chemical Engineering Dynamics [[electronic resource] ] : Modelling with PC Simulation |
| Autore | Ingham John |
| Pubbl/distr/stampa | Hoboken, : Wiley, 2008 |
| Descrizione fisica | 1 online resource (670 p.) |
| Disciplina |
660.28
660.28155362 |
| Altri autori (Persone) |
DunnIrving J
HeinzleElmar PrenosilJiri E |
| Soggetto topico |
Bond graphs
Chemical engineering -- Computer simulation Chemical engineering -- Mathematical models Thermodynamics |
| ISBN |
1-281-75883-3
9786611758837 3-527-61601-2 3-527-61600-4 |
| Formato | Materiale a stampa  |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
Chemical Engineering Dynamics; Preface; Organisation of the Book; Acknowledgements; Table of Contents; Nomenclature for Chapters 1 to 4; 1 Basic Concepts; 1.1 Modelling Fundamentals; 1.1.1 Chemical Engineering Modelling; 1.1.2 General Aspects of the Modelling Approach; 1.1.3 General Modelling Procedure; 1.2 Formulation of Dynamic Models; 1.2.1 Material Balance Equations; 1.2.2 Balancing Procedures; 1.2.2.1 Case A . Continuous Stirred-Tank Reactor; 1.2.2.2 Case B . Tubular Reactor; 1.2.2.3 Case C . Coffee Percolator; 1.2.3 Total Material Balances; 1.2.3.1 Case A . Tank Drainage
1.2.4 Component Balances1.2.4.1 Case A . Waste Holding Tank; 1.2.4.2 Case B . Extraction from a Solid by a Solvent; 1.2.5 Energy Balancing; 1.2.5.1 Case A . Continuous Heating in an Agitated Tank; 1.2.5.2 Case B . Heating in a Filling Tank; 1.2.5.3 Case C . Parallel Reaction in a Semi-Continuous Reactor with Large Temperature Changes; 1.2.6 Momentum Balances; 1.2.7 Dimensionless Model Equations; 1.2.7.1 Case A . Continuous Stirred-Tank Reactor (CSTR); 1.2.7.2 Case B . Gas-Liquid Mass Transfer to a Continuous Tank Reactor with Chemical Reaction; 1.3 Chemical Kinetics 1.3.1 Rate of Chemical Reaction1.3.2 Reaction Rate Constant; 1.3.3 Heats of Reaction; 1.3.4 Chemical Equilibrium and Temperature; 1.3.5 Yield, Conversion and Selectivity; 1.4 Microbial Growth Kinetics; 1.5 Mass Transfer Theory; 1.5.1 Stagewise and Differential Mass Transfer Contacting; 1.5.2 Phase Equilibria; 1.5.3 Interphase Mass Transfer; 2 Process Dynamics Fundamentals; 2.1 Signal and Process Dynamics; 2.1.1 Measurement and Process Response; 2.1.1.1 First-Order Response to an Input Step-Change Disturbance; 2.1.1.2 Case A . Concentration Response of a Continuous Flow, Stirred Tank 2.1.1.3 Case B . Concentration Response in a Continuous Stirred Tank with Chemical Reaction2.1.1.4 Case C . Response of a Temperature Measuring Element; 2.1.1.5 Case D . Measurement Lag for Concentration in a Batch Reactor; 2.1.2 Higher-order Responses; 2.1.2.1 Case A . Multiple Tanks in Series; 2.1.2.2 Case B . Response of a Second-Order Temperature Measuring Element; 2.1.3 Pure Time Delay; 2.1.4 Transfer Function Representation; 2.2 Time Constants; 2.2.1 Common Time Constants; 2.2.1.1 Flow Phenomena; 2.2.1.2 Diffusion and Dispersion; 2.2.1.3 Chemical Reaction; 2.2.1.4 Mass Transfer 2.2.1.5 Heat Transfer2.2.2 Application of Time Constants; 2.3 Fundamentals of Automatic Control; 2.3.1 Basic Feedback Control; 2.3.2 Types of Controller Action; 2.3.2.1 On/Off Control; 2.3.2.2 Proportional-Integral-Derivative (PID) Control; 2.3.2.3 Case A . Operation of a Proportional Temperature Controller; 2.3.3 Controller Tuning; 2.3.3.1 Trial and Error Method; 2.3.3.2 Ziegler-Nichols Method; 2.3.3.3 Cohen-Coon Controller Settings; 2.3.3.4 Ultimate Gain Method; 2.3.3.5 Time Integral Criteria; 2.3.4 Advanced Control Strategies; 2.3.4.1 Cascade Control; 2.3.4.2 Feedforward Control 2.3.4.3 Adaptive Control |
| Record Nr. | UNINA-9910144329803321 |
Ingham John
|
||
| Hoboken, : Wiley, 2008 | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||
Chemical Engineering Dynamics [[electronic resource] ] : Modelling with PC Simulation
| Chemical Engineering Dynamics [[electronic resource] ] : Modelling with PC Simulation |
| Autore | Ingham John |
| Pubbl/distr/stampa | Hoboken, : Wiley, 2008 |
| Descrizione fisica | 1 online resource (670 p.) |
| Disciplina |
660.28
660.28155362 |
| Altri autori (Persone) |
DunnIrving J
HeinzleElmar PrenosilJiri E |
| Soggetto topico |
Bond graphs
Chemical engineering -- Computer simulation Chemical engineering -- Mathematical models Thermodynamics |
| ISBN |
1-281-75883-3
9786611758837 3-527-61601-2 3-527-61600-4 |
| Formato | Materiale a stampa |
| Livello bibliografico | Monografia |
| Lingua di pubblicazione | eng |
| Nota di contenuto |
Chemical Engineering Dynamics; Preface; Organisation of the Book; Acknowledgements; Table of Contents; Nomenclature for Chapters 1 to 4; 1 Basic Concepts; 1.1 Modelling Fundamentals; 1.1.1 Chemical Engineering Modelling; 1.1.2 General Aspects of the Modelling Approach; 1.1.3 General Modelling Procedure; 1.2 Formulation of Dynamic Models; 1.2.1 Material Balance Equations; 1.2.2 Balancing Procedures; 1.2.2.1 Case A . Continuous Stirred-Tank Reactor; 1.2.2.2 Case B . Tubular Reactor; 1.2.2.3 Case C . Coffee Percolator; 1.2.3 Total Material Balances; 1.2.3.1 Case A . Tank Drainage
1.2.4 Component Balances1.2.4.1 Case A . Waste Holding Tank; 1.2.4.2 Case B . Extraction from a Solid by a Solvent; 1.2.5 Energy Balancing; 1.2.5.1 Case A . Continuous Heating in an Agitated Tank; 1.2.5.2 Case B . Heating in a Filling Tank; 1.2.5.3 Case C . Parallel Reaction in a Semi-Continuous Reactor with Large Temperature Changes; 1.2.6 Momentum Balances; 1.2.7 Dimensionless Model Equations; 1.2.7.1 Case A . Continuous Stirred-Tank Reactor (CSTR); 1.2.7.2 Case B . Gas-Liquid Mass Transfer to a Continuous Tank Reactor with Chemical Reaction; 1.3 Chemical Kinetics 1.3.1 Rate of Chemical Reaction1.3.2 Reaction Rate Constant; 1.3.3 Heats of Reaction; 1.3.4 Chemical Equilibrium and Temperature; 1.3.5 Yield, Conversion and Selectivity; 1.4 Microbial Growth Kinetics; 1.5 Mass Transfer Theory; 1.5.1 Stagewise and Differential Mass Transfer Contacting; 1.5.2 Phase Equilibria; 1.5.3 Interphase Mass Transfer; 2 Process Dynamics Fundamentals; 2.1 Signal and Process Dynamics; 2.1.1 Measurement and Process Response; 2.1.1.1 First-Order Response to an Input Step-Change Disturbance; 2.1.1.2 Case A . Concentration Response of a Continuous Flow, Stirred Tank 2.1.1.3 Case B . Concentration Response in a Continuous Stirred Tank with Chemical Reaction2.1.1.4 Case C . Response of a Temperature Measuring Element; 2.1.1.5 Case D . Measurement Lag for Concentration in a Batch Reactor; 2.1.2 Higher-order Responses; 2.1.2.1 Case A . Multiple Tanks in Series; 2.1.2.2 Case B . Response of a Second-Order Temperature Measuring Element; 2.1.3 Pure Time Delay; 2.1.4 Transfer Function Representation; 2.2 Time Constants; 2.2.1 Common Time Constants; 2.2.1.1 Flow Phenomena; 2.2.1.2 Diffusion and Dispersion; 2.2.1.3 Chemical Reaction; 2.2.1.4 Mass Transfer 2.2.1.5 Heat Transfer2.2.2 Application of Time Constants; 2.3 Fundamentals of Automatic Control; 2.3.1 Basic Feedback Control; 2.3.2 Types of Controller Action; 2.3.2.1 On/Off Control; 2.3.2.2 Proportional-Integral-Derivative (PID) Control; 2.3.2.3 Case A . Operation of a Proportional Temperature Controller; 2.3.3 Controller Tuning; 2.3.3.1 Trial and Error Method; 2.3.3.2 Ziegler-Nichols Method; 2.3.3.3 Cohen-Coon Controller Settings; 2.3.3.4 Ultimate Gain Method; 2.3.3.5 Time Integral Criteria; 2.3.4 Advanced Control Strategies; 2.3.4.1 Cascade Control; 2.3.4.2 Feedforward Control 2.3.4.3 Adaptive Control |
| Record Nr. | UNINA-9910831171703321 |
|
Ingham John
|
||
| Hoboken, : Wiley, 2008 | ||
| Materiale a stampa | ||
| Lo trovi qui: Univ. Federico II | ||
| ||