Chemical Process: Design and Integration 1st Edition by Robin Smith – Ebook PDF Instant Download/Delivery: 0471486817, 978-0471486817
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ISBN 10: 0471486817
ISBN 13: 978-0471486817
Author: Robin Smith
Chemical Process Design and Integration 1st 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
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
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
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
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
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
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
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
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
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
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
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
Chapter 14: Continuous Process Recycle Structure
14.1 The Function of Process Recycles
14.2 Recycles with Purges
14.3 Hybrid Reaction and Separation
14.4 The Process Yield
14.5 Feed, Product and Intermediate Storage
14.6 Continuous Process Recycle Structure – Summary
14.7 Exercises
Chapter 15: Continuous Process Simulation and Optimization
15.1 Physical Property Models for Process Simulation
15.2 Unit Models for Process Simulation
15.3 Flowsheet Models
15.4 Simulation of Recycles
15.5 Convergence of Recycles
15.6 Design Specifications
15.7 Flowsheet Sequencing
15.8 Model Validation
15.9 Process Optimization
15.10 Continuous Process Simulation and Optimization – Summary
Chapter 16: Batch Processes
16.1 Characteristics of Batch Processes
16.2 Batch Reactors
16.3 Batch Distillation
16.4 Batch Crystallization
16.5 Batch Filtration
16.6 Batch Heating and Cooling
16.7 Optimization of Batch Operations
16.8 Gantt Charts
16.9 Production Schedules for Single Products
16.10 Production Schedules for Multiple Products
16.11 Equipment Cleaning and Material Transfer
16.12 Synthesis of Reaction and Separation Systems for Batch Processes
16.13 Storage in Batch Processes
16.14 Batch Processes – Summary
16.15 Exercises
Chapter 17: Heat Exchanger Networks I – Network Targets
17.1 Composite Curves
17.2 The Heat Recovery Pinch
17.3 Threshold Problems
17.4 The Problem Table Algorithm
17.5 Non-Global Minimum Temperature Differences
17.6 Process Constraints
17.7 Utility Selection
17.8 Furnaces
17.9 Cogeneration (Combined Heat and Power Generation)
17.10 Integration of Heat Pumps
17.11 Number of Heat Exchange Units
17.12 Heat Exchange Area Targets
17.13 Sensitivity of Targets
17.14 Capital and Total Cost Targets
17.15 Heat Exchanger Network Targets – Summary
17.16 Exercises
Chapter 18: Heat Exchanger Networks II – Network Design
18.1 The Pinch Design Method
18.2 Design for Threshold Problems
18.3 Stream Splitting
18.4 Design for Multiple Pinches
18.5 Remaining Problem Analysis
18.6 Simulation of Heat Exchanger Networks
18.7 Optimization of a Fixed Network Structure
18.8 Automated Methods of Heat Exchanger Network Design
18.9 Heat Exchanger Network Retrofit with a Fixed Network Structure
18.10 Heat Exchanger Network Retrofit through Structural Changes
18.11 Automated Methods of Heat Exchanger Network Retrofit
18.12 Heat Exchanger Network Design – Summary
Chapter 19: Heat Exchanger Networks III – Stream Data
19.1 Process Changes for Heat Integration
19.2 The Trade-Offs Between Process Changes, Utility Selection, Energy Cost and Capital Cost
19.3 Data Extraction
19.4 Heat Exchanger Network Stream Data – Summary
19.5 Exercises
Chapter 20: Heat Integration of Reactors
20.1 The Heat Integration Characteristics of Reactors
20.2 Appropriate Placement of Reactors
20.3 Use of the Grand Composite Curve for Heat Integration of Reactors
20.4 Evolving Reactor Design to Improve Heat Integration
20.5 Heat Integration of Reactors – Summary
20.6 Exercises
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