Chemical Process Design and Integration 2nd Edition by Robin Smith ISBN 1119990130 9781119990130

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ISBN 10: 1119990130 
ISBN 13: 9781119990130
Author: Robin Smith

Written by a highly regarded author with industrial and academic experience, this new edition of an established bestselling book provides practical guidance for students, researchers, and those in chemical engineering. The book includes a new section on sustainable energy, with sections on carbon capture and sequestration, as a result of increasing environmental awareness; and a companion website that includes problems, worked solutions, and Excel spreadsheets to enable students to carry out complex calculations.

Chemical Process Design and Integration 2nd Table of contents:

Chapter 1: The Nature of Chemical Process Design and Integration 1.1 Chemical Products
1.2 Formulation of Design Problems
1.3 Synthesis and Simulation
1.4 The Hierarchy of Chemical Process Design and Integration
1.5 Continuous and Batch Processes
1.6 New Design and Retrofit
1.7 Reliability, Availability and Maintainability
1.8 Process Control
1.9 Approaches to Chemical Process Design and Integration
1.10 The Nature of Chemical Process Design and Integration – Summary
References

Chapter 2: Process Economics
2.1 The Role of Process Economics
2.2 Capital Cost for New Design
2.3 Capital Cost for Retrofit
2.4 Annualized Capital Cost
2.5 Operating Cost
2.6 Simple Economic Criteria
2.7 Project Cash Flow and Economic Evaluation
2.8 Investment Criteria
2.9 Process Economics — Summary
2.10 Exercises
References

Chapter 3: Optimization
3.1 Objective Functions
3.2 Single-Variable Optimization
3.3 Multivariable Optimization
3.4 Constrained Optimization
3.5 Linear Programming
3.6 Nonlinear Programming
3.7 Structural Optimization
3.8 Solution of Equations Using Optimization
3.9 The Search for Global Optimality
3.10 Optimization – Summary
3.11 Exercises
References

Chapter 4: Chemical Reactors I – Reactor Performance
4.1 Reaction Path
4.2 Types of Reaction Systems
4.3 Measures of Reactor Performance
4.4 Rate of Reaction
4.5 Idealized Reactor Models
4.6 Choice of Idealized Reactor Model
4.7 Choice of Reactor Performance
4.8 Reactor Performance – Summary
4.9 Exercises
References

Chapter 5: Chemical Reactors II – Reactor Conditions
5.1 Reaction Equilibrium
5.2 Reactor Temperature
5.3 Reactor Pressure
5.4 Reactor Phase
5.5 Reactor Concentration
5.6 Biochemical Reactions
5.7 Catalysts
5.8 Reactor Conditions – Summary
5.9 Exercises
References

Chapter 6: Chemical Reactors III – Reactor Configuration
6.1 Temperature Control
6.2 Catalyst Degradation
6.3 Gas–Liquid and Liquid–Liquid Reactors
6.4 Reactor Configuration
6.5 Reactor Configuration For Heterogeneous Solid-Catalyzed Reactions
6.6 Reactor Configuration – Summary
6.7 Exercises
References

Chapter 7: Separation of Heterogeneous Mixtures
7.1 Homogeneous and Heterogeneous Separation
7.2 Settling and Sedimentation
7.3 Inertial and Centrifugal Separation
7.4 Electrostatic Precipitation
7.5 Filtration
7.6 Scrubbing
7.7 Flotation
7.8 Drying
7.9 Separation of Heterogeneous Mixtures – Summary
7.10 Exercises
References

Chapter 8: Separation of Homogeneous Fluid Mixtures I – Distillation
8.1 Vapor–Liquid Equilibrium
8.2 Calculation of Vapor-Liquid Equilibrium
8.3 Single-Stage Separation
8.4 Distillation
8.5 Binary Distillation
8.6 Total and Minimum Reflux Conditions for Multicomponent Mixtures
8.7 Finite Reflux Conditions for Multicomponent Mixtures
8.8 Column Dimensions
8.9 Conceptual Design of Distillation
8.10 Detailed Design of Distillation
8.11 Limitations of Distillation
8.12 Separation of Homogeneous Fluid Mixtures by Distillation – Summary
8.13 Exercises
References

Chapter 9: Separation of Homogeneous Fluid Mixtures II – Other Methods
9.1 Absorption and Stripping
9.2 Liquid–Liquid Extraction
9.3 Adsorption
9.4 Membranes
9.5 Crystallization
9.6 Evaporation
9.7 Separation of Homogeneous Fluid Mixtures by Other Methods – Summary
Exercises
References

Chapter 10: Distillation Sequencing
10.1 Distillation Sequencing using Simple Columns
10.2 Practical Constraints Restricting Options
10.3 Choice of Sequence for Simple Nonintegrated Distillation Columns
10.4 Distillation Sequencing using Columns With More Than Two Products
10.5 Distillation Sequencing using Thermal Coupling
10.6 Retrofit of Distillation Sequences
10.7 Crude Oil Distillation
10.8 Structural Optimization of Distillation Sequences
10.9 Distillation Sequencing – Summary
Exercises
References

Chapter 11: Distillation Sequencing for Azeotropic Distillation
11.1 Azeotropic Systems
11.2 Change in Pressure
11.3 Representation of Azeotropic Distillation
11.4 Distillation at Total Reflux Conditions
11.5 Distillation at Minimum Reflux Conditions
11.6 Distillation at Finite Reflux Conditions
11.7 Distillation Sequencing Using an Entrainer
11.8 Heterogeneous Azeotropic Distillation
11.9 Entrainer Selection
11.10 Multicomponent Systems
11.11 Trade-Offs in Azeotropic Distillation
11.12 Membrane Separation
11.13 Distillation Sequencing for Azeotropic Distillation – Summary
Exercises
References

Chapter 12: Heat Exchange
12.1 Overall Heat Transfer Coefficients
12.2 Heat Exchanger Fouling
12.3 Temperature Differences in Shell-and-Tube Heat Exchangers
12.4 Heat Exchanger Geometry
12.5 Allocation of Fluids in Shell-and-Tube Heat Exchangers
12.6 Heat Transfer Coefficients and Pressure Drops in Shell-and-Tube Heat Exchangers
12.7 Rating and Simulation of Heat Exchangers
12.8 Heat Transfer Enhancement
12.9 Retrofit of Heat Exchangers
12.10 Condensers
12.11 Reboilers and Vaporizers
12.12 Other Types of Heat Exchangers
12.13 Fired Heaters
12.14 Heat Exchange – Summary
Exercises
References

Chapter 13: Pumping and Compression
13.1 Pressure Drops in Process Operations
13.2 Pressure Drops in Piping Systems
13.3 Pump Types
13.4 Centrifugal Pump Performance
13.5 Compressor Types
13.6 Reciprocating Compressors
13.7 Dynamic Compressors
13.8 Staged Compression
13.9 Compressor Performance
13.10 Process Expanders
13.11 Pumping and Compression – Summary
13.12 Exercises

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