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    Optimization of

    Chemical Processes

    Cheng-Liang ChenPSELABORATORY

    Department of Chemical EngineeringNational TAIWAN University

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    Chen CL 1

    Optimization of Chemical Processes (cont.)

    The chemical industry has undergone significant changes duringthe past 25 years due to the

    increased cost of energy,

    increasingly stringent environmental regulations, and

    global competition in product pricing and quality

    One of the most important engineering tools for addressing these

    issues is optimization

    Modifications in plant design and operating procedures havebeen implemented to reduce costs and meet constraints, with

    an emphasis on improving efficiencyand increasing profitability

    Optimal operating conditionscan be implemented via increasedautomation at the process, plant, and company levels

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    Contents of Arora (cont.)

    Introduction to Optimum Design Conventional versus Optimum Design Processes Role of Computers in Optimum Design Basic Terminology and Notations

    Optimum Design Problem Formulation

    Design Variables, Cost Function, and Design Constraints Examples of Optimum Design Problem Formulation

    Optimum Design Concepts

    Fundamental Concepts

    Unconstrained Optimum Design Problems Constrained Optimum Design Problems Global Optimality Post-optimality Analysis

    C C

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    Contents of Arora (cont.)

    Linear Programming Definition of Standard LP Problems Basic Concepts Related to LP Problems The Simplex Method Initial Basic Feasible Solution Artificial Variables Post-optimality Analysis

    Numerical Methods for Unconstrained Optimization

    General Concepts Related to Numerical Algorithms One-dimensional Minimization Steepest Descent Method

    Conjugate Gradient Method Newtons Method Quasi-Newton Methods

    Ch CL 6

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    Contents of Arora (cont.)

    Numerical Methods for Constrained Optimization Basic Concepts and Ideas Sequential Unconstrained Optimization Algorithm Linearization of Constrained Problem

    Sequential Linear Programming AlgorithmsQuadratic Programming Subproblem

    Constrained Steepest Descent Method Constrained Quasi-Newton Methods

    Interactive Design Optimization

    Practical Design Optimization

    Ch CL 7

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    Contents of Floudas (cont.) Introduction

    Mathematical and Optimization Models Structure of Nonlinear and Mixed-Integer Optimization Models Illustrative Applications

    Part 1: Fundamentals of Convex Analysis and Nonlinear

    Optimization

    Convex Analysis

    Convex Sets Convex and Concave Functions

    Fundamentals of Nonlinear Optimization

    Unconstrained Nonlinear Optimization Constrained Nonlinear Optimization

    Duality Theory

    Primal Problem

    Dual Problem

    Ch CL 8

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    Contents of Floudas (cont.)

    Part 2: Fundamentals of Mixed-Integer Optimization Mixed-Integer Linear Optimization

    Motivation and Formulation Branch and Bound Method

    Mixed-Integer Nonlinear Optimization Motivation and Formulation Generalized Benders Decomposition (GBD) Outer Approximations (OA)

    Outer Approximations with Equality Relaxation (OA/ER)

    Outer Approximations with Equality Relaxation and Augmented Penalty(OA/ER/AP)

    Generalized Outer Approximations (GOA) Generalized Cross Decomposition (GCD)

    Ch CL 9

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    Contents of Floudas (cont.)

    Part 3: Applications in Process Synthesis Process Synthesis

    Difficulties/Challenges in Process Synthesis Optimization Approach in Process Synthesis

    Heat Exchanger Network Synthesis

    Distillation-based Separation Systems Synthesis

    Synthesis of Reactor Networks and Reactor-Separator-

    Recycle Systems

    Chen CL 10

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    Contents of Floudas Global Optimization

    Introduction; Basic concepts of Global Optimization

    The BB Box Constrained Twice-diff. NLPs: Theory

    The BB Constrained Twice-diff. NLPs: Theory

    Computational Studies of The BB Approach

    Introduction to Nonlinear and Mixed-integer Optimization

    The SMIN-BB Approach: Theory and Computations

    The GMIN-BB Approach: Theory and Computations

    Chen CL 11

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    Contents of Edgar (cont.)I Problem Formulation

    The Nature and Organization of Optimization Problems Developing Models for Optimization

    Formulation of the Objective Function

    II Optimization Theory and Methods

    Basic Concepts of Optimization Optimization of Unconstrained Functions: One-Dimensional

    Search

    Unconstrained Multi-variable Optimization

    Linear Programming and Applications

    Nonlinear Programming with Constraints

    Mixed-Integer Programming

    Global Optimization for Problems with Continuous andDiscrete Variables

    Chen CL 12

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    Contents of Edgar (cont.)

    III Applications of Optimization

    Hear Transfer and Energy Conservation

    Separation Processes

    Fluid Flow Systems

    Chemical Reactor Design and Operation

    Optimization in Large-Scale Plant Design and Operations

    Integrated Planning, Scheduling, and Control in the ProcessIndustries

    Chen CL 13

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    Contents of Biegler (cont.)

    Introduction to Process DesignI Preliminary Analysis and Evaluation of Processes

    Overview of Flowsheet Synthesis

    Mass and Energy Balances

    Equipment Sizing and Costing

    Economic Evaluation

    Dsign and Scheduling of Batch Processes

    II Analysis with Rigorous Process Models

    Unit Equation Models

    General Concepts of Simulation for Process Design

    Process Flowsheet Optimization

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    Contents of Biegler (cont.)

    IV Optimization Approaches to Process Synthesis

    Basic Concepts for Algorithmic Methods

    Synthesis of Heat Exchange Networks

    Synthesis of Distillation Sequences

    Simultaneous Optimization and Heat Integration

    Optimization Techniques for Reactor Network Syntheses

    Structural Optimization of Process Flowsheets Process Flexibility

    Optimal Design and Scheduling for Multiproduct Batch

    Plants

    Chen CL 16

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    Contents of Smith (cont.)

    The Nature of Chemical Process Design and Integration Process Economics

    Optimization

    Thermodynamic Properties and Phase Equilibrium

    Choice of Reactor I Reactor Performance

    Choice of Reactor II Reactor Conditions

    Choice of Reactor III Reactor configuration

    Choice of Separator for Heterogeneous Mixtures

    Choice of Separator for Homogeneous Fluid Mixtures I Distillation

    Choice of Separator for Homogeneous Fluid Mixtures II Other Methods

    Distillation Sequencing

    Distillation Sequencing for Azeotropic Distillation

    Reaction, Separation and Recycle Systems for Continuous Processes

    Reaction, Separation and Recycle Systems for Batch Processes

    Chen CL 17

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    Contents of Smith (cont.)

    Heat Exchanger Networks I Heat Transfer Equipment

    Heat Exchanger Networks II Energy Targets

    Heat Exchanger Networks III Capital and Total Cost Targets

    Heat Exchanger Networks IV Network Design

    Heat Exchanger Networks V Stream Data

    Heat Integration of Reactors

    Heat Integration of Distillation Columns

    Heat Integration of Evaporators and Dryers

    Steam Systems and Cogeneration

    Cooling and Refrigeration Environmental Design for Atmospheric Emissions

    Water System Design

    Inherent Safety

    Clean Process Technology

    Overall Strategy for Chemical Process Design and Integration

    Chen CL 18

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    Case Studies Using GAMS (cont.)

    Refinery Scheduling Production Planning in Multi-purpose Batch Plants

    LP Model for Minimizing Utility Cost in A Heat Exchanger Network

    Logical Inference for Reaction Path Synthesis

    Design of A Chemical Complex Multi-product Batch Plant Scheduling

    Multi-period MILP Model for Planning of Chemical Complexes

    Power Generation via Fuel Oil

    Alkylation Process Optimization Chemical Equilibrium

    Multi-Component Phase Equilibrium

    Global Optimum Search in Heat Exchanger Network Configurations

    Chen CL 19

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    Case Studies Using GAMS (cont.)

    Optimal Selection of Processes Optimal Design of Multi-product Batch Plants

    Simultaneous Optimization Model for Heat Exchanger Network Synthesis

    Heat Integrated Distillation Sequences

    Non-sharp Distillation Synthesis Optimum Feed Plate Location

    Minimum Time to Cover A Fixed Distance

    Catalyst Mixing for Packed Bed Reactor

    Parameter Estimation for A Simple Batch Reactor System

    Chen CL 20

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    Course OutlinesArora Floudas/Biegler Edgar MATLAB GAMS

    Int to Optimum Design Problems

    Problem Formulation Math and Opt Models ModelsOptimum DesignConcepts

    Convex Analysis;

    Fundamentals of Nonlinear Opt;

    Duality Theory

    Linear Programming ** * ***

    MILP; Logical Constraints * ****

    Num. Unconst. Opt. * ** *

    Num. Const. Opt. * ** **

    MINLP; Process Synthesis * ***

    Global Optimization

    Some Special Topics: Smith

    Synthesis of Heat/Mass Exchanger Networks (include Pinch Analysis)

    Synthesis of Water Networks, Cooling Water Networks

    Batch Scheduling; Supply Chain Management; . . .

    Chen CL 21

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    Credits

    5 8 Homeworks (40%)

    Mid-term Examination (25%)

    Final Examination (25%)

    Oral Presentation of Assigned Materials (10%)