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[資源]
Distillation Design and Control Using AspenTM Simulation--Second Edition高清版
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免責(zé)聲明：本資料僅供個人學(xué)習(xí)、研究之用，嚴禁用于任何商業(yè)目的，請下載后自覺在6小時內(nèi)自行刪除。如違反，由此引起的一切后果均由其本人承擔(dān)，本人不承擔(dān)任何責(zé)任或相關(guān)、連帶責(zé)任！ Table of Contents Preface xi 1 Fundamentals of Vapor-Liquid Phase Equilibrium (VLE) 1 1.1 Vapor Pressure 1 1.2 Binary VLE Phase Diagrams 3 1.3 Physical Property Methods 7 1.4 Relative Volatility 7 1.5 Bubblepoint Calculations 9 1.6 Ternary Diagrams 10 1.7 VLE Nonideality 12 1.8 Residue Curves for Ternary Systems 18 1.9 Conclusion 26 2 Analysis of Distillation Columns 27 2.1 Design Degrees of Freedom 27 2.2 Binary McCabe-Thiele Method 28 2.3 Approximate Multicomponent Methods 38 2.4 Analysis of Ternary Systems Using DISTIL 41 2.5 Conclusion 44 3 Setting up a Steady-State Simulation 45 3.1 Configuring a New Simulation 45 3.2 Specifying Chemical Components and Physical Properties 53 3.3 Specifying Stream Properties 58 3.4 Specifying Equipment Parameters 60 3.5 Running the Simulation 64 3.6 Using "Design Spec/Vary" Function 66 3.7 Finding the Optimum Feed Tray and Minimum Conditions 80 3.8 Column Sizing 81 3.9 Conclusion 84 4 Distillation Economic Optimization 85 4.1 Heuristic Optimization 85 4.2 Economic Basis 87 4.3 Results 89 4.4 Operating Optimization 91 4.5 Conclusion 97 5 More Complex Distillation Systems 98 5.1 Methyl Acetate/Methanol/Water System 98 5.2 Ethanol Dehydration 112 5.3 Heat-Integrated Columns 122 5.4 Conclusion 129 6 Steady-State Calculations for Control Structure Selection 130 6.1 Summary of Methods 131 6.2 Binary Propane/Isobutane System 133 6.3 Ternary BTX System 137 6.4 Multicomponent Hydrocarbon System 141 6.5 Ternary Azeotropic System 145 6.6 Conclusion 150 7 Converting From Steady State to Dynamic Simulation 151 7.1 Equipment Sizing 151 7.2 Exporting to Aspen Dynamics 153 7.3 Opening the Dynamic Simulation in Aspen Dynamics 156 7.4 Installing Basic Controllers 158 7.5 Installing Temperature and Composition Controllers 166 7.6 Performance Evaluation 179 7.7 Comparison with Economic Optimum Design 184 7.8 Conclusion 187 8 Control of More Complex Columns 188 8.1 Methyl Acetate Column 188 8.2 Columns with Partial Condensers 190 8.3 Control of Heat-Integrated Distillation Columns 209 8.4 Control of Azeotropic Columns/Decanter System 222 8.5 Conclusion 231 9 Reactive Distillation 232 9.1 Introduction 232 9.2 Types of Reactive Distillation Systems 234 9.3 TAME Process Basics 238 9.4 TAME Reaction Kinetics and VLE 241 9.5 Plantwide Control Structure 246 9.6 Conclusion 250 10 Control of Sidestream Columns 251 10.1 Liquid Sidestream Column 252 10.2 Vapor Sidestream Column 257 10.3 Liquid Sidestream Column with Stripper 264 10.4 Vapor Sidestream Column with Rectifier 271 10.5 Sidestream Purge Column 281 10.6 Conclusion 290 11 Control of Petroleum Fractionators 291 11.1 Petroleum Fractions 292 11.2 Characterization of Crude Oil 296 11.3 Steady-State Design of PREFLASH Column 304 11.4 Control of PREFLASH Column 311 11.5 Steady-State Design of Pipestill 316 11.6 Control of Pipestill 333 11.7 Conclusion 342 Index 343 下載地址： 鏈接: http://pan.baidu.com/s/1i3moY3r 密碼: 3hs9 |
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