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Process dynamics and control : modeling for control and prediction /

Detalles Bibliográficos
Autor principal: Roffel, Brian
Otros Autores: Betlem, B. H. (Ben H.)
Formato: Libro
Lenguaje:English
Publicado: Chichester, England ; Hoboken, NJ : John Wiley & Sons, c2006.
Materias:
Acceso en línea:Table of contents only
Contributor biographical information
Publisher description
Beschreibung für Leser
Inhaltsverzeichnis

MARC

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245 1 0 |a Process dynamics and control :  |b modeling for control and prediction /  |c Brian Roffel and Ben Betlem. 
260 |a Chichester, England ;  |a Hoboken, NJ :  |b John Wiley & Sons,  |c c2006. 
300 |a xv, 543 páginas :  |b ilustraciones ;  |c 25 cm. 
504 |a Incluye bibliografía e índice. 
505 1 |a CONTENTS -- FOREWORD -- PREFACE -- ACKNOWLEDGEMENT -- 1 Introduction to Process Modeling -- 1.1 Application of Process Models -- 1.2 Dynamic Systems Modeling -- 1.3 Modeling Steps -- 1.4 Use of Diagrams -- 1.5 Types of Model -- 1.6 Continuous versus Discrete Models -- References -- 2 Process Modeling Fundamentals -- 2.1 System States -- 2.2 Mass Relationship for Liquid and Gas -- 2.3 Energy Relationship -- 2.4 Composition Relationship -- 3 Extended Analysis of Modeling for Process Operation -- 3.1 Environmental Model -- 3.2 Procedure for the Development of an Environmental Model for Process Operation -- 3.3 Example: Mixer -- 3.4 Example: Evaporator with Variable Heat Exchanging Surface -- 4 Design for Process Modeling and Behavioral Models -- 4.1 Behavioral Model -- 4.2 Example: A Mixer -- 5 Transformation Techniques -- 5.1 Introduction -- 5.2 Laplace Transform -- 5.3 Useful Properties of Laplace Transform: limit functions -- 5.4 Transfer Functions -- 5.5 Discrete Approximations -- 5.6 z-Transforms -- References -- 6 Linearization of Model Equations -- 6.1 Introduction -- 6.2 Non-linear Process Models -- 6.3 Some General Linearization Rules -- 6.4 Linearization of Model of the Level Process -- 6.5. Linearization of the Evaporator Model -- 6.6 Normalization of the Transfer Function -- 6.7. Linearization of the Chemical Reactor Model -- 7 Operating points -- 7.1 Introduction -- 7.2 Stationary System and Operating Point -- 7.3 Flow Systems -- 7.4 Chemical System -- 7.5 Stability in the Operating Point -- 7.6 Operating Point Transition -- 8 Process Simulation -- 8.1 Using Matlab Simulink -- 8.2 Simulation of the Level Process -- 8.3 Simulation of the Chemical Reactor -- References -- 9 Frequency Response Analysis -- 9.1 Introduction -- 9.2 Bode Diagrams -- 9.3 Bode Diagram of Simulink Models -- References -- 10 General Process Behavior -- 10.1 Introduction -- 10.2 Accumulation Processes -- 10.3 Lumped Process with Non-interacting Balances -- 10.4 Lumped Process with Interacting Balances -- 10.5 Processes with Parallel Balances -- 10.6 Distributed Processes -- 10.7 Processes with Propagation without Feedback -- 10.8 Processes with Propagation with Feedback -- 11 Analysis of a Mixing Process -- 11.1 The Process -- 11.2 Mixer with Self-adjusting Height -- 12 Dynamics of Chemical Stirred Tank Reactors -- 12.1 Introduction -- 12.2 Isothermal First-order Reaction -- 12.3 Equilibrium Reactions -- 12.4 Consecutive Reactions -- 12.5 Non-isothermal Reactions -- 13 Dynamic Analysis of Tubular Reactors -- 13.1 Introduction -- 13.2 First-order Reaction -- 13.3 Equilibrium Reaction -- 13.4 Consecutive Reactions -- 13.5 Tubular Reactor with Dispersion -- 13.6 Dynamics of Adiabatic Tubular Flow Reactors -- References -- 14 Dynamic Analysis of Heat Exchangers -- 14.1 Introduction -- 14.2 Heat Transfer from -- 
650 4 |a Control de procesos químicos.  |9 358430 
700 1 |a Betlem, B. H.  |q (Ben H.). 
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856 4 |3 Beschreibung für Leser  |u http://catdir.loc.gov/catdir/enhancements/fy0740/2006019140-d.html 
856 4 1 |3 Inhaltsverzeichnis  |u http://catdir.loc.gov/catdir/toc/ecip0615/2006019140.html 
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