LEADER 05229nam 2200625 450 001 9910144002903321 005 20230721030212.0 010 $a1-281-23930-5 010 $a9786611239305 010 $a3-527-61421-4 010 $a3-527-61422-2 035 $a(CKB)1000000000376068 035 $a(EBL)481339 035 $a(SSID)ssj0000291300 035 $a(PQKBManifestationID)11245812 035 $a(PQKBTitleCode)TC0000291300 035 $a(PQKBWorkID)10250084 035 $a(PQKB)10333016 035 $a(MiAaPQ)EBC481339 035 $a(MiAaPQ)EBC6913652 035 $a(Au-PeEL)EBL6913652 035 $a(OCoLC)184983896 035 $a(EXLCZ)991000000000376068 100 $a20221013d2007 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 10$aChemical engineering dynamics $ean introduction to modelling and computer simulation /$fJohn Ingham, [and five others] 205 $a3rd, completely rev. ed. 210 1$aWeinheim, Germany :$cWiley-VCH GmbH,$d[2007] 210 4$dİ2007 215 $a1 online resource (643 p.) 300 $aIncludes index. 311 $a3-527-31678-7 320 $aIncludes bibliographical references and index. 327 $aChemical Engineering Dynamics; Contents; Preface; Acknowledgements; Nomenclature for Chapters 1-4; 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 Balances 327 $a1.2.4.1 Case A: Waste Holding Tank1.2.4.2 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 Reaction 327 $a1.3.2 Reaction Rate Constant1.3.3 Heat of Reaction; 1.3.4 Chemical Equilibrium and Temperature; 1.3.5 Yield, Conversion and Selectivity; 1.3.6 Microbial Growth Kinetics; 1.4 Mass Transfer Theory; 1.4.1 Stagewise and Differential Mass Transfer Contacting; 1.4.2 Phase Equilibria; 1.4.3 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 327 $a2.1.1.3 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-Dispersion; 2.2.1.3 Chemical Reaction; 2.2.1.4 Mass Transfer 327 $a2.2.1.5 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 Open-Loop 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 327 $a2.3.4.3 Adaptive Control 330 $aIn this book, the modelling of dynamic chemical engineering processes is presented in a highly understandable way using the unique combination of simplified fundamental theory and direct hands-on computer simulation. The mathematics is kept to a minimum, and yet the nearly 100 examples supplied on a CD-ROM illustrate almost every aspect of chemical engineering science. Each example is described in detail, including the model equations. They are written in the modern user-friendly simulation language Berkeley Madonna, which can be run on both Windows PC and Power-Macintosh computers.Mad 606 $aChemical engineering$xMathematical models 615 0$aChemical engineering$xMathematical models. 676 $a660.28155362 700 $aIngham$b John$cDr.,$021598 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910144002903321 996 $aChemical engineering dynamics$92041672 997 $aUNINA