Exercises have been added at the end of each chapter to allow the reader to practice the calculation procedures.
- The Nature of Chemical Process Design and Integration
- Chemical Products
- Formulation of the Design Problem
- Chemical Process Design and Integration
- The Hierarchy of Chemical Process Design and Integration
- Continuous and Batch Processes
- New Design and Retrofit
- Approaches to Chemical Process Design and Integration
- Process Control
- The Nature of Chemical Process Design and Integration – Summary
- Process Economics
- The Role of Process Economics
- Capital Cost for New Design
- Capital Cost for Retrofit
- Annualized Capital Cost
- Operating Cost
- Simple Economic Criteria
- Project Cash Flow and Economic Evaluation
- Investment Criteria
- Process Economics – Summary
- Optimization
- Objective Functions
- Single-variable Optimization
- Multivariable Optimization
- Constrained Optimization
- Linear Programming
- Nonlinear Programming
- Profile Optimization
- Structural Optimization
- Solution of Equations using Optimization
- The Search for Global Optimality
- Summary – Optimization
- Thermodynamic Properties and Phase Equilibrium
- Equations of State
- Phase Equilibrium for Single Components
- Fugacity and Phase Equilibrium
- Vapor–Liquid Equilibrium
- Vapor–Liquid Equilibrium Based on Activity Coefficient Models
- Vapor–Liquid Equilibrium Based on Equations of State
- Calculation of Vapor–Liquid Equilibrium
- Liquid–Liquid Equilibrium
- Liquid–Liquid Equilibrium Activity Coefficient Models
- Calculation of Liquid–Liquid Equilibrium
- Calculation of Enthalpy
- Calculation of Entropy
- Phase Equilibrium and Thermodynamic Properties – Summary
- Choice of Reactor I – Reactor Performance
- Reaction Path
- Types of Reaction Systems
- Reactor Performance
- Rate of Reaction
- Idealized Reactor Models
- Choice of Idealized Reactor Model
- Choice of Reactor Performance
- Choice of Reactor Performance – Summary
- Choice of Reactor II – Reactor Conditions
- Reaction Equilibrium
- Reactor Temperature
- Reactor Pressure
- Reactor Phase
- Reactor Concentration
- Biochemical Reactions
- Catalysts
- Choice of Reactor Conditions – Summary
- Choice of Reactor III – Reactor Configuration
- Temperature Control
- Catalyst Degradation
- Gas–Liquid and Liquid–Liquid Reactors
- Reactor Configuration
- Reactor Configuration for Heterogeneous Solid-Catalyzed Reactions
- Reactor Configuration from Optimization of a Superstructure
- Choice of Reactor Configuration – Summary
- Choice of Separator for Heterogeneous Mixtures
- Homogeneous and Heterogeneous Separation
- Settling and Sedimentation
- Inertial and Centrifugal Separation
- Electrostatic Precipitation
- Filtration
- Scrubbing
- Flotation
- Drying
- Separation of Heterogeneous Mixtures – Summary
- Choice of Separator for Homogeneous Fluid Mixtures I – Distillation
- Single-Stage Separation
- Distillation
- Binary Distillation
- Total and Minimum Reflux Conditions for Multicomponent Mixtures
- Finite Reflux Conditions for Multicomponent Mixtures
- Choice of Operating Conditions
- Limitations of Distillation
- Separation of Homogeneous Fluid Mixtures by Distillation – Summary
- Choice of Separator for Homogeneous Fluid Mixtures II – Other Methods
- Absorption and Stripping
- Liquid–Liquid Extraction
- Adsorption
- Membranes
- Crystallization
- Evaporation
- Separation of Homogeneous Fluid Mixtures by Other Methods – Summary
- Distillation Sequencing
- Distillation Sequencing Using Simple Columns
- Practical Constraints Restricting Options
- Choice of Sequence for Simple Nonintegrated Distillation Columns
- Distillation Sequencing Using Columns With More Than Two Products
- Distillation Sequencing Using Thermal Coupling
- Retrofit of Distillation Sequences
- Crude Oil Distillation
- Distillation Sequencing Using Optimization of a Superstructure
- Distillation Sequencing – Summary
- Distillation Sequencing for Azeotropic Distillation
- Azeotropic Systems
- Change in Pressure
- Representation of Azeotropic Distillation
- Distillation at Total Reflux Conditions
- Distillation at Minimum Reflux Conditions
- Distillation at Finite Reflux Conditions
- Distillation Sequencing Using an Entrainer
- Heterogeneous Azeotropic Distillation
- Entrainer Selection
- Trade-offs in Azeotropic Distillation
- Multicomponent Systems
- Membrane Separation
- Distillation Sequencing for Azeotropic Distillation – Summary
- Reaction, Separation and Recycle Systems for Continuous Processes
- The Function of Process Recycles
- Recycles with Purges
- Pumping and Compression
- Simulation of Recycles
- The Process Yield
- Optimization of Reactor Conversion
- Optimization of Processes Involving a Purge
- Hybrid Reaction and Separation
- Feed, Product and Intermediate Storage
- Reaction, Separation and Recycle Systems for Continuous Processes – Summary
- Reaction, Separation and Recycle Systems for Batch Processes
- Batch Processes
- Batch Reactors
- Batch Separation Processes
- Gantt Charts
- Production Schedules for Single Products
- Production Schedules for Multiple Products
- Equipment Cleaning and Material Transfer
- Synthesis of Reaction and Separation Systems for Batch Processes
- Optimization of Batch Processes
- Storage in Batch Processes
- Reaction and Separation Systems for Batch Processes – Summary
- Heat Exchanger Networks I – Heat Transfer Equipment
- Overall Heat Transfer Coefficients
- Heat Transfer Coefficients and Pressure Drops for Shell-and-Tube Heat Exchangers
- Temperature Differences in Shell-and-Tube Heat Exchangers
- Allocation of Fluids in Shell-and-Tube Heat Exchangers
- Extended Surface Tubes
- Retrofit of Heat Exchangers
- Condensers
- Reboilers and Vaporizers
- Other Types of Heat Exchange Equipment
- Fired Heaters
- Heat Transfer Equipment – Summary
- Heat Exchanger Networks II – Energy Targets
- Composite Curves
- The Heat Recovery Pinch
- Threshold Problems
- The Problem Table Algorithm
- Nonglobal Minimum Temperature Differences
- Process Constraints
- Utility Selection
- Furnaces
- Cogeneration (Combined Heat and Power Generation)
- Integration Of Heat Pumps
- Heat Exchanger Network Energy Targets – Summary
- Heat Exchanger Networks III – Capital and Total Cost Targets
- Number of Heat Exchange Units
- Heat Exchange Area Targets
- Number-of-shells Target
- Capital Cost Targets
- Total Cost Targets
- Heat Exchanger Network and Utilities Capital and Total Costs – Summary
- Heat Exchanger Networks IV – Network Design
- The Pinch Design Method
- Design for Threshold Problems
- Stream Splitting
- Design for Multiple Pinches
- Remaining Problem Analysis
- Network Optimization
- The Superstructure Approach to Heat Exchanger Network Design
- Retrofit of Heat Exchanger Networks
- Addition of New Heat Transfer Area in Retrofit
- Heat Exchanger Network Design – Summary
- Heat Exchanger Networks V – Stream Data
- Process Changes for Heat Integration
- The Trade-Offs Between Process Changes, Utility Selection, Energy Cost and Capital Cost
- Data Extraction
- Heat Exchanger Network Stream Data – Summary
- Heat Integration of Reactors
- The Heat Integration Characteristics of Reactors
- Appropriate Placement of Reactors
- Use of the Grand Composite Curve for Heat Integration of Reactors
- Evolving Reactor Design to Improve Heat Integratio
- Heat Integration of Reactors – Summary
- Heat Integration of Distillation Columns
- The Heat Integration Characteristics of Distillation
- The Appropriate Placement of Distillation
- Use of the Grand Composite Curve for Heat Integration of Distillation
- Evolving the Design of Simple Distillation Columns to Improve Heat Integration
- Heat Pumping in Distillation
- Capital Cost Considerations
- Heat Integration Characteristics of Distillation Sequences
- Heat-integrated Distillation Sequences Based on the Optimization of a Superstructure
- Heat Integration of Distillation Columns – Summary
- Heat Integration of Evaporators and Dryers
- The Heat Integration Characteristics of Evaporators
- Appropriate Placement of Evaporators
- Evolving Evaporator Design to Improve Heat Integration
- The Heat Integration Characteristics of Dryers
- Evolving Dryer Design to Improve Heat Integration
- Heat Integration of Evaporators and Dryers – Summary
- Steam Systems and Cogeneration
- Boiler Feedwater Treatment
- Steam Boilers
- Steam Turbines
- Gas Turbines
- Steam System Configuration
- Steam and Power Balances
- Site Composite Curves
- Cogeneration Targets
- Optimization of Steam Levels
- Site Power-to-heat Ratio
- Optimizing Steam Systems
- Steam Costs
- Choice of Driver
- Steam Systems and Cogeneration – Summary
- Cooling and Refrigeration Systems
- Cooling Systems
- Recirculating Cooling Water Systems
- Targeting Minimum Cooling Water Flowrate
- Design of Cooling Water Networks
- Retrofit of Cooling Water Systems
- Refrigeration Cycles
- Process Expanders
- Choice of Refrigerant for Compression Refrigeration
- Targeting Refrigeration Power for Compression Refrigeration
- Heat Integration of Compression Refrigeration Processes
- Mixed Refrigerants for Compression Refrigeration
- Absorption Refrigeration
- Indirect Refrigeration
- Cooling Water and Refrigeration Systems – Summary
- Environmental Design for Atmospheric Emissions
- Atmospheric Pollution
- Sources of Atmospheric Pollution
- Control of Solid Particulate Emissions to Atmosphere
- Control of VOC Emissions to Atmosphere
- Control of Sulfur Emissions
- Control of Oxides of Nitrogen Emissions
- Control of Combustion Emissions
- Atmospheric Dispersion
- Environmental Design for Atmospheric Emissions – Summary
- Water System Design
- Aqueous Contamination
- Primary Treatment Processes
- Biological Treatment Processes
- Tertiary Treatment Processes
- Water Use
- Targeting Maximum Water Reuse for Single Contaminants
- Design for Maximum Water Reuse for Single Contaminants
- Targeting and Design for Maximum Water Reuse Based on Optimization of a Superstructure
- Process Changes for Reduced Water Consumption
- Targeting Minimum Wastewater Treatment Flowrate for Single Contaminants
- Design for Minimum Wastewater Treatment Flowrate for Single Contaminants
- Regeneration of Wastewater
- Targeting and Design for Effluent Treatment and Regeneration Based on Optimization of a Superstructure
- Data Extraction
- Water System Design – Summary
- Inherent Safety
- Fire
- Explosion
- Toxic Release
- Intensification of Hazardous Materials
- Attenuation of Hazardous Materials
- Quantitative Measures of Inherent Safety
- Inherent Safety – Summary
- Clean Process Technology
- Sources of Waste from Chemical Production
- Clean Process Technology for Chemical Reactors
- Clean Process Technology for Separation and Recycle Systems
- Clean Process Technology for Process Operations
- Clean Process Technology for Utility Systems
- Trading off Clean Process Technology Options
- Life Cycle Analysis
- Clean Process Technology – Summary
- Overall Strategy for Chemical Process Design and Integration
- Objectives
- The Hierarchy
- The Final Design
Appendix A: Annualization of Capital Cost
Appendix B: Gas Compression
- Reciprocating Compressors
- Centrifugal Compressors
- Staged Compression
Appendix C: Heat Transfer Coefficients and Pressure Drop in Shell-and-tube Heat Exchangers
- Pressure Drop and Heat Transfer Correlations for the Tube-Side
- Pressure Drop and Heat Transfer Correlations for the Shell-Side
Appendix D: The Maximum Thermal Effectiveness for 1–2 Shell-and-tube Heat Exchangers
Appendix E: Expression for the Minimum Number of 1–2 Shell-and-tube Heat Exchangers for a Given Unit
Appendix F: Algorithm for the Heat Exchanger Network Area Target
Appendix G: Algorithm for the Heat Exchanger Network Number of Shells Target
- Minimum Area Target for Networks of 1–2 Shells
Appendix H: Algorithm for Heat Exchanger Network Capital Cost Targets
Index