Chemical reactors design and control (Record no. 43963)
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| 000 -LEADER | |
|---|---|
| fixed length control field | 07021nam a2200241Ia 4500 |
| 003 - CONTROL NUMBER IDENTIFIER | |
| control field | OSt |
| 005 - DATE AND TIME OF LATEST TRANSACTION | |
| control field | 20260602104409.0 |
| 008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION | |
| fixed length control field | 210219s9999||||xx |||||||||||||| ||und|| |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER | |
| ISBN | 9780470097700 |
| 082 ## - DEWEY DECIMAL CLASSIFICATION NUMBER | |
| Classification number | 660.28425 LNY-C |
| 100 ## - MAIN ENTRY--AUTHOR NAME | |
| Personal name | Luyben, William L |
| 245 #0 - TITLE STATEMENT | |
| Title | Chemical reactors design and control |
| 260 ## - PUBLICATION, DISTRIBUTION, ETC. (IMPRINT) | |
| Place of publication | New Jersey: |
| Name of publisher | JWS, |
| Year of publication | 2007. |
| 300 ## - PHYSICAL DESCRIPTION | |
| Number of Pages | xvi, 419p. |
| 520 ## - SUMMARY, ETC. | |
| Summary, etc | Table of Contents<br/>Preface.<br/>Chapter 1. Reactor Basics.<br/><br/>1.1 Fundamentals of Reaction Equilibrium and Kinetics.<br/><br/>1.1.1 Power-Law Kinetics.<br/><br/>1.1.2 Heterogeneous Reaction Kinetics.<br/><br/>1.1.3 Biochemical Reaction Kinetics.<br/><br/>1.1.4 References.<br/><br/>1.2 Multiple Reactions.<br/><br/>1.2.1 Parallel Reactions.<br/><br/>1.2.2 Series Reactions.<br/><br/>1.3 Determining Kinetic Parameters.<br/><br/>1.4 Types and Fundamental Properties of Reactors.<br/><br/>1.4.1 Continuous Stirred-Tank Reactor.<br/><br/>1.4.2 Batch Reactor.<br/><br/>1.4.3 Tubular Plug-Flow Reactor.<br/><br/>1.5 Heat Transfer in Reactors.<br/><br/>1.6 Reactor Scale-Up.<br/><br/>1.7 Conclusion.<br/><br/>Chapter 2. Steady-State Design of CSTR Systems.<br/><br/>2.1 Irreversible, Single Reactant.<br/><br/>2.1.1 Jacket Cooled.<br/><br/>2.1.2 Internal Coil.<br/><br/>2.1.3 Other Issues.<br/><br/>2.2 Irreversible, Two Reactants.<br/><br/>2.2.1 Equations.<br/><br/>2.2.2 Design.<br/><br/>2.3 Reversible Exothermic.<br/><br/>2.4 Consecutive Reactions.<br/><br/>2.5 Simultaneous Reactions.<br/><br/>2.6 Multiple CSTR’s.<br/><br/>2.6.1 Multiple Isothermal CSTR’s in Series with Reaction A-B.<br/><br/>2.6.2 Multiple CSTR’s in Series with Different Temperatures.<br/><br/>2.6.3 Multiple CSTR’s in Parallel.<br/><br/>2.6.4 Multiple CSTR’s with Reversible Exothermic Reactions.<br/><br/>2.7 Auto-Refrigerated Reactor.<br/><br/>2.8 Aspen Plus Simulation of CSTR’s.<br/><br/>2.8.1 Simulation Setup.<br/><br/>2.8.2 Specifying Reactions.<br/><br/>2.8.3 Reactor Setup.<br/><br/>2.9 Optimization of CSTR Systems.<br/><br/>2.9.1 Economics of Series CSTR’s.<br/><br/>2.9.2 Economics of a Reactor/Column Process.<br/><br/>2.9.3 CSTR Processes with Two Reactants.<br/><br/>2.10 Conclusion.<br/><br/>Chapter 3. Control of CSTR Systems.<br/><br/>3.1 Irreversible, Single Reactant.<br/><br/>3.1.1 Nonlinear Dynamic Model.<br/><br/>3.1.2 Linear Model.<br/><br/>3.1.3 Effect of Conversion on Openloop and Closedloop Stability.<br/><br/>3.1.4 Nonlinear Dynamic Simulation.<br/><br/>3.1.5 Effect of Jacket Volume.<br/><br/>3.1.6 Cooling Coil.<br/><br/>3.1.7 External Heat Exchanger.<br/><br/>3.1.8 Comparison of CSTR-in-Series Processes.<br/><br/>3.1.9 Dynamics of Reactor/Stripper Process.<br/><br/>3.2 Reactor/Column Process with Two Reactants.<br/><br/>3.2.1 Nonlinear Dynamic Model of Reactor and Column.<br/><br/>3.2.2 Control Structure for Reactor/Column Process.<br/><br/>3.2.3 Reactor/Column Process with Hot Reaction.<br/><br/>3.3 Auto-Refrigerated Reactor Control.<br/><br/>3.3.1 Dynamic Model.<br/><br/>3.3.2 Simulation Results.<br/><br/>3.4 Reactor Temperature Control Using Feed Manipulation.<br/><br/>3.4.1 Introduction.<br/><br/>3.4.2 Revised Control Structure.<br/><br/>3.4.3 Results.<br/><br/>3.4.4 Valve-Position Control.<br/><br/>3.5 Aspen Dynamics Simulation of CSTR’s.<br/><br/>3.5.1 Setting Up the Dynamic Simulation.<br/><br/>3.5.2 Running the Simulation and Tuning Controllers.<br/><br/>3.5.3 Results with Several Heat-Transfer Options.<br/><br/>3.6 Conclusion.<br/><br/>Chapter 4. Control of Batch Reactors.<br/><br/>4.1 Irreversible, Single Reactant.<br/><br/>4.1.1 Pure Batch Reactor.<br/><br/>4.1.2 Fed-Batch Reactor.<br/><br/>4.2 Batch Reactor with Two Reactants.<br/><br/>4.3 Batch Reactor with Consecutive Reactions.<br/><br/>4.4 Aspen Plus Simulation using RBatch.<br/><br/>4.5 Ethanol Batch Fermentor.<br/><br/>4.6 Fed-Batch Hydrogenation Reactor.<br/><br/>4.7 Batch TML Reactor.<br/><br/>4.8 Fed-Batch Reactor with Multiple Reactions.<br/><br/>4.8.1 Equations.<br/><br/>4.8.2 Effect of Feed Trajectory on Conversion and Selectivity.<br/><br/>4.8.3 Batch Optimization.<br/><br/>4.8.4 Effect of Parameters.<br/><br/>4.8.5 Simultaneous Reaction Case.<br/><br/>4.9 Conclusion.<br/><br/>Chapter 5. Steady-State Design of Tubular Reactor Systems.<br/><br/>5.1 Introduction.<br/><br/>5.2 Types of Tubular Reactor Systems.<br/><br/>5.2.1 Type of Recycle.<br/><br/>5.2.2 Phase of Reaction.<br/><br/>5.2.3 Heat-Transfer Configuration.<br/><br/>5.3 Tubular Reactors in Isolation.<br/><br/>5.3.1 Adiabatic PFR.<br/><br/>5.3.2 Non-Adiabatic PFR.<br/><br/>5.4 Single Adiabatic Tubular Reactor System with Gas Recycle.<br/><br/>5.4.1 Process Conditions and Assumptions.<br/><br/>5.4.2 Design and Optimization Procedure.<br/><br/>5.4.3 Results for Single Adiabatic Reactor System.<br/><br/>5.5 Multiple Adiabatic Tubular Reactors with Interstage Cooling.<br/><br/>5.5.1 Design and Optimization Procedure.<br/><br/>5.5.2 Results for Multiple Adiabatic Reactors with Interstage Cooling.<br/><br/> 5.6 Multiple Adiabatic Tubular Reactors with Cold-Shot Cooling.<br/><br/>5.6.1 Design and Optimization Procedure.<br/><br/>5.6.2 Results for Multiple Adiabatic Reactors with Cold-Shot Cooling.<br/><br/>5.7 Cooled Reactor System.<br/><br/>5.7.1 Design Procedure for Cooled Reactor System.<br/><br/>5.7.2 Results for Cooled Reactor System.<br/><br/>5.8 Tubular Reactor Simulation using Aspen Plus.<br/><br/>5.8.1 Adiabatic Tubular Reactor.<br/><br/>5.8.2 Cooled Tubular Reactor with Constant Temperature Coolant.<br/><br/>5.8.3 Cooled Reactor with Co-Current or Counter-Current Coolant Flow.<br/><br/>5.9 Conclusion.<br/><br/>Chapter 6. Control of Tubular Reactor Systems.<br/><br/>6.1 Introduction.<br/><br/>6.2 Dynamic Model.<br/><br/>6.3 Control Structures.<br/><br/>6.4 Controller Tuning and Disturbances.<br/><br/>6.5 Results for Single Adiabatic Reactor System.<br/><br/>6.6 Multi-Stage Adiabatic Reactor System with Interstage Cooling.<br/><br/>6.7 Multi-Stage Adiabatic Reactor System with Cold-Shot Cooling.<br/><br/>6.8 Cooled Reactor System.<br/><br/>6.9 Cooled Reactor System with Hot Reaction.<br/><br/>6.9.1 Steady-State Design.<br/><br/>6.9.2 Openloop and Closedloop Responses.<br/><br/>6.9.3 Conclusion.<br/><br/>6.10 Aspen Dynamics Simulation.<br/><br/>6.10.1 Adiabatic Reactor with and without Catalyst.<br/><br/>6.10.2 Cooled Reactor with Coolant Temperature Manipulated.<br/><br/>6.10.3 Cooled Reactor with Co-Current Flow of Coolant.<br/><br/>6.10.4 Cooled Reactor with Counter-Current Flow of Coolant.<br/><br/>6.10.5 Conclusions for Aspen Simulation of Types of Tubular Reactors.<br/><br/>6.11 Plantwide Control of Methanol Process.<br/><br/>6.11.1 Chemistry and Kinetics.<br/><br/>6.11.2 Process Description.<br/><br/>6.11.3 Steady-State Aspen Plus Simulation.<br/><br/>6.11.4 Dynamic Simulation.<br/><br/>6.12 Conclusion .<br/><br/>Chapter 7. Feed-Effluent Heat Exchangers.<br/><br/>7.1 Introduction.<br/><br/>7.2 Steady-State Design.<br/><br/>7.3 Linear Analysis.<br/><br/>7.31 Flowsheet FS1 without Furnace.<br/><br/>7.3.2 Flowsheet FS2 with Furnace.<br/><br/>7.3.3 Nyquist Plots.<br/><br/>7.4 Nonlinear Simulation.<br/><br/>7.4.1 Dynamic Model.<br/><br/>7.4.2 Control Structure.<br/><br/>7.4.3 Results.<br/><br/>7.5. Hot Reaction Case.<br/><br/>7.6 Aspen Simulation.<br/><br/>7.7 Conclusion.<br/><br/>Chapter 8. Control of Special Types of Industrial Reactors.<br/><br/>8.1 Fluidized Catalytic Crackers.<br/><br/>8.1.2 Reactor.<br/><br/>8.1.2 Regenerator.<br/><br/>8.1.3 Control Issues.<br/><br/>8.2 Gasifiers.<br/><br/>8.3 Fired Furnaces, Kilns and Driers.<br/><br/>8.4 Pulp Digesters.<br/><br/>8.5 Polymerization Reactors.<br/><br/>8.6 Biochemical Reactors.<br/><br/>8.7 Slurry Reactors.<br/><br/>8.8 Micro-Scale Reactors. |
| 650 ## - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical Term | Chemical reactors |
| 650 ## - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical Term | Chemical process control |
| 650 ## - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical Term | Chemical engineering |
| 650 ## - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical Term | Reaction kinetics |
| 650 ## - SUBJECT ADDED ENTRY--TOPICAL TERM | |
| Topical Term | Process control |
| 942 ## - ADDED ENTRY ELEMENTS (KOHA) | |
| Koha item type | Reference |
| Full call number | Accession Number | Koha item type | Lost status | Damaged status | Permanent Location | Current Location | Shelving location | Date acquired |
|---|---|---|---|---|---|---|---|---|
| 660.28425 LNY-C | 82714 | Reference | Central Library, NIT Jalandhar | Central Library, NIT Jalandhar | Reference | 20.02.2021 |