Sustainable design through process integration : fundamentals and applications to industrial pollution prevention, resource conservation, and profitability enhancement /
Sustainable Design through Process Integration: Fundamentals and Applications to Industrial Pollution Prevention, Resource Conservation, and Profitability Enhancement, Third Edition provides authoritative, comprehensive, and easy-to-follow coverage of the fundamental concepts and practical technique...
| Main Author: | |
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| Corporate Author: | |
| Format: | eBook |
| Language: | English |
| Published: |
Amsterdam :
Elsevier,
2025.
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| Edition: | Third edition. |
| Subjects: | |
| Online Access: | Connect to the full text of this electronic book |
Table of Contents:
- Front Cover
- Sustainable Design Through Process Integration
- Copyright Page
- Dedication
- Contents
- About the Author
- Preface
- 1 Introduction to Sustainability, Sustainable Design, and Process Integration
- 1.1 What Is Sustainability?
- 1.2 What Is Sustainable Design through Process Integration?
- 1.3 Process Design Phases
- 1.4 Motivating Examples on the Generation and Integration of Sustainable-Design Alternatives
- 1.4.1 Motivating Example on Process Improvement and Debottlenecking
- 1.4.2 Motivating Example on Heat Integration
- 1.4.3 Motivating Example on Generation and Screening of Chemical Pathways for a New Design
- 1.5 Structure and Learning Outcomes of the Book
- References
- 2 Overview of Process Economics
- 2.1 Introduction
- 2.2 Cost Types and Estimation
- 2.2.1 Capital Cost Estimation
- 2.2.1.1 Manufacturer's Quotation
- 2.2.1.2 Computer-Aided Tools
- 2.2.1.3 Capacity Ratio with Exponent
- 2.2.1.3.1 Updates Using Cost Indices
- 2.2.1.3.2 Ratio Factors Based on Delivered Equipment Cost
- 2.2.1.3.3 Empirical Correlations
- 2.2.1.3.4 Natural/Shale Gas-Conversion Plants
- 2.2.1.3.5 Biorefineries
- 2.2.1.3.6 Turnover Ratio
- 2.2.2 Equipment-Cost Estimation
- 2.2.2.1 Manufacturer's Quotation
- 2.2.2.2 Computer-Aided Tools
- 2.2.2.3 Capacity Ratio with Exponent
- 2.2.2.4 Updates Using Cost Indices
- 2.2.2.5 Cost Charts
- 2.2.3 Operating-Cost or Operating-Expenditure (OPEX) Estimation
- 2.2.4 Production-Cost Estimation
- 2.3 Depreciation
- 2.3.1 Linear Depreciation (Straight-Line Method)
- 2.3.2 Declining-Balance Method
- 2.3.3 Modified Accelerated Cost Recovery System
- 2.4 Break-Even Analysis
- 2.5 Time Value of Money
- 2.5.1 Compound Interest of a Single Payment
- 2.5.2 Cash Flow Diagram
- 2.5.3 Annuities
- 2.6 Profitability Analysis.
- 2.6.1 Profitability Criteria without the Time-Value of Money
- 2.6.1.1 Payback Period
- 2.6.2 Profitability Criteria with the Time-Value of Money
- 2.6.2.1 Net Present Value (NPV) or Net Present Worth (NPW)
- 2.6.2.2 Discounted Cash Flow Return on Investment (Internal Rate of Return)
- 2.6.2.3 Discounted Payback Period
- 2.6.3 Comparison of Alternatives
- 2.6.3.1 Net Present Value (Net Present Worth)
- 2.6.3.2 Annual Cost/Revenue
- 2.6.3.3 Total Annualized Cost
- 2.6.3.4 Incremental Return on Investment (IROI)
- 2.7 Inclusion of Sustainability and Targeting in Profitability Calculations: Sustainability Return on Investment
- 2.8 Homework Problems
- References
- 3 Mass-Integration Benchmarking of New Designs via Stoichiometric Targeting
- 3.1 What Is Benchmarking?
- 3.2 Stoichiometric Targeting
- 3.3 Stoichiometric-Economic "Stoichio-Nomic" Targeting
- 3.4 A Shortcut Approach to Using Stoichiometric Targeting for Creating and Screening Initial Designs
- 3.5 Homework Problems
- References
- 4 Process-Improvement Benchmarking of Existing Designs via Mass-Integration Targeting
- 4.1 Scope of Process-Improvement Mass-Integration Targeting
- 4.2 Process-Improvement Mass-Integration Targeting
- 4.2.1 Targeting for Minimum Waste Discharge
- 4.2.2 Targeting for Minimum Purchase of Fresh Material Utilities
- 4.2.3 Targeting for Maximum Product Yield
- 4.3 Detailing Mass Integration Strategies for Attaining Process-Improvement Targets
- 4.3.1 Homework Problems
- References
- 5 Direct-Recycle Networks: Graphical and Algebraic Targeting Approaches
- 5.1 Problem Statement for the Design of Direct-Recycle Networks
- 5.2 Selection of Sources, Sinks, and Recycle Routes
- 5.3 Direct-Recycle Targets through Material-Recycle Pinch Diagram
- 5.4 Design Rules from the Material-Recycle Pinch Diagram.
- 5.5 Extension to the Case of Impure Fresh
- 5.6 Insights for Process Modifications
- 5.7 An Algebraic Approach to Targeting Direct Recycle Networks
- 5.8 Algebraic Targeting Procedure
- 5.9 Generating Implementation Designs Using the Source-Sink Mapping Diagram for Matching Sources and Sinks
- 5.10 Multicomponent Source-Sink Mapping Diagram
- 5.11 Homework Problems
- Nomenclature
- Superscripts
- Subscripts
- Greek Letters
- References
- 6 Synthesis of Mass-Exchange Networks
- 6.1 Mass-Exchange Network Synthesis Task
- 6.2 The Men-Targeting Approach
- 6.2.1 Minimum Cost of MSAs
- 6.2.2 Minimum Number of Mass Exchanger Units
- 6.3 The Corresponding Composition Scales
- 6.4 The Mass-Exchange Pinch Diagram
- 6.5 Constructing Pinch Diagrams Without Process MSAs
- 6.6 An Algebraic Approach to Targeting Mass-Exchange Networks
- 6.6.1 The Composition-Interval Diagram
- 6.6.2 Table of Exchangeable Loads
- 6.6.3 Mass-Exchange Cascade Diagram
- 6.7 Construction of the Men Configuration with Minimum Number of Exchangers
- 6.7.1 Feasibility Criteria at the Pinch
- 6.7.1.1 Stream Population
- 6.7.2 Operating Line versus Equilibrium Line
- 6.7.3 Network Synthesis
- 6.8 Trading Off Fixed Cost versus Operating Cost
- 6.8.1 Trading off Fixed and Operating Costs by Varying the Mass-Exchange Driving Forces
- 6.8.2 Trading off Fixed and Operating Costs by Mixing Rich Streams
- 6.8.3 Trading off Fixed and Operating Costs Using Mass-Load Paths
- 6.9 PROBLEMS
- Symbols
- Greek
- References
- 7 Combining Mass-Integration Strategies
- 7.1 Process Representation from a Mass-Integration Species Perspective
- 7.2 Homework Problems
- References
- 8 Heat Integration
- 8.1 Heat-Exchange Network-Synthesis Problem Statement
- 8.2 Minimum Utility Targets via the Thermal Pinch Diagram.
- 8.3 Minimum Utility Targets Using the Algebraic Cascade Diagram
- 8.4 Screening of Multiple Utilities Using the Grand Composite Representation
- 8.5 Stream Matching and the Synthesis of Heat-Exchange Networks
- 8.5.1 Stream Population Rules for Matching
- 8.5.2 Flowrate Specific Heat Rules for Matching
- 8.6 Homework Problems
- Symbols
- Greek
- References
- 9 Integration of Combined Heat and Power Systems
- 9.1 heat Engines
- 9.2 Steam Turbines and Power Plants
- 9.3 Placement of Heat Engines and Integration with Thermal Pinch Analysis
- 9.4 Heat Pumps
- 9.5 Closed-Cycle Vapor Compression Heat Pumps Using a Separate Working Fluid (Refrigerant)
- 9.5.1 Description and Modeling of a Heat Pump
- 9.5.2 Dual-Mode Heat Pumps
- 9.6 vapor-Compression Heat Pumps and Thermal Pinch Diagram
- 9.7 Open-Cycle Mechanical Vapor Recompression Using a Process Stream as the Working Fluid
- 9.8 Absorption Refrigeration Cycles
- 9.9 Cogeneration Targeting
- 9.10 Additional Readings
- 9.11 Homework Problems
- References
- 10 Property Integration
- 10.1 Property-Based Material Recycle Pinch Diagram
- 10.2 Process Modification Based on Property-Based Pinch Diagram
- 10.3 Clustering Techniques for Multiple Properties
- 10.4 Cluster-Based Source-Sink Mapping Diagram for Property-Based Recycle and Interception
- 10.5 Property-Based Design Rules for Recycle and Interception
- 10.5.1 Source Prioritization Rule
- 10.5.2 Lever Arm Source Prioritization Rule
- 10.6 Dealing with Multiplicity of Cluster-To-Property Mapping
- 10.7 Relationship between Clusters and Mass Fractions
- 10.8 Additional Readings
- 10.9 Homework
- Nomenclature
- Subscripts
- Superscripts
- Greek Letters
- References
- 11 Overview of Optimization
- 11.1 What Is Mathematical Programming?
- 11.2 How to Formulate an Optimization Model?.
- 11.3 Using the Software Lingo to Solve Optimization Problems
- 11.4 Interpreting Dual Prices in the Results of a Lingo Solution
- 11.5 A Brief Introduction to Sets, Convex Analysis, and Symbols Used in Optimization
- 11.5.1 Sets
- 11.5.2 Convex Analysis
- 11.5.3 Symbols Used in Optimization Formulations
- 11.6 the Use of 0-1 Binary-Integer Variables
- 11.7 Enumerating Multiple Solutions Using Integer Cuts
- 11.8 Modeling Disjunctions and Discontinuous Functions with Binary Integer Variables
- 11.8.1 Discontinuous Functions
- 11.8.2 Big-M Reformulation
- 11.8.3 Convex-Hull Reformulation
- 11.9 Using Set Formulations in LINGO
- 11.9.1 Summation
- 11.9.2 Defining Sets
- 11.9.3 Entering Data
- 11.9.4 The @FOR Command
- 11.9.5 Dealing with Double Summations
- 11.9.6 Entering Two-Dimensional Data
- 11.9.7 Using @FOR in the Case of Repeating Constraints with Two-Dimensional Variables
- 11.9.8 Adding Logical Operators
- 11.10 Homework Problems
- References
- 12 An Optimization Approach to Direct Recycle
- 12.1 PROBLEM STATEMENT
- 12.2 Problem Representation
- 12.3 Optimization Formulation
- 12.4 Additional Readings
- 12.5 Homework Problems
- References
- 13 Synthesis of Mass-Exchange Networks: A Mathematical Programming Approach
- 13.1 Generalization of the Composition Interval Diagram
- 13.2 Problem Formulation
- 13.3 Optimization of Outlet Compositions
- 13.4 Stream Matching and Network Synthesis
- 13.4 Problems
- Symbols
- References
- 14 Synthesis of Reactive Mass-Exchange Networks
- 14.1 Objectives of REAMEN Synthesis
- 14.2 Corresponding Composition Scales for Reactive Mass Exchange
- 14.3 Synthesis Approach
- 14.4 Homework Problems
- Symbols
- Greek Letters
- Special Symbol
- References
- 15 Mathematical Optimization Techniques for Mass Integration
- 15.1 Problem Statement and Challenges.