Smith:

Chemical Process: Design and Integration

Instructor Companion Site

Table Of Contents

Chapter 1: The Nature of Chemical Process Design and Integration

Chapter 2: Process Economics

Chapter 3: Optimization

Chapter 4: Thermodynamic Properties and Phase Equilibrium

Chapter 5: Choice of Reactor I – Reactor Performance

Chapter 6: Choice of Reactor II – Reactor Conditions

Chapter 7: Choice of Reactor III – Reactor Configuration

Chapter 8: Choice of Separator for Heterogeneous Mixtures

Chapter 9: Choice of Separator for Homogeneous Fluid Mixtures I – Distillation

Chapter 10: Choice of Separator for Homogeneous Fluid Mixtures II – Other Methods

Chapter 11: Distillation Sequencing

Chapter 12: Distillation Sequencing for Azeotropic Distillation

Chapter 13: Reaction, Separation and Recycle Systems for Continuous Processes

Chapter 14: Reaction, Separation and Recycle Systems for Batch Processes

Chapter 15: Heat Exchanger Networks I – Heat Transfer Equipment

Chapter 16: Heat Exchanger Networks II – Energy Targets

Chapter 17: Heat Exchanger Networks III – Capital and Total Cost Targets

Chapter 18: Heat Exchanger Networks IV – Network Design

Chapter 19: Heat Exchanger Networks V – Stream Data

Chapter 20: Heat Integration of Reactors

Chapter 21: Heat Integration of Distillation Columns

Chapter 22: Heat Integration of Evaporators and Dryers

Chapter 23: Steam Systems and Cogeneration

Chapter 24: Cooling and Refrigeration Systems

Chapter 25: Environmental Design for Atmospheric Emissions

Chapter 26: Water System Design

Chapter 27: Inherent Safety

Chapter 28: Clean Process Technology

Appendix B: Gas Compression

Appendix C: Heat Transfer Coefficients and Pressure Drop in Shell-and-tube Heat Exchangers

Appendix F: Algorithm for the Heat Exchanger Network Area Target

Appendix G: Algorithm for the Heat Exchanger Network Number of Shells Target

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