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9780824795610

Applied Parameter Estimation for Chemical Engineers

by ;
  • ISBN13:

    9780824795610

  • ISBN10:

    082479561X

  • Edition: 1st
  • Format: Hardcover
  • Copyright: 2000-10-12
  • Publisher: CRC Press

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Summary

A reference and textbook providing readers with the most important optimization methods for parameter estimation in chemical engineering. The CD-ROM features Fortran computer programs for solving equation systems and other problems with Microsoft Excel and Sigma Plot. Contains over 900 equations in all.

Author Biography

Peter Englezos is Professor in the Department of Chemical and Biological Engineering, University of British Columbia, Vancouver, Canada Nicolas Kalogerakis is Professor of Biochemical Engineering and Director of the Laboratory of Biochemical Engineering and Environmental Biotechnology, Department of Environmental Engineering, Technical University of Crete, Chania, Greece

Table of Contents

Preface v
Introduction
1(6)
Formulation of the Parameter Estimation Problem
7(16)
Structure of the Mathematical Model
7(6)
Algebraic Equation Models
7(4)
Differential Equation Models
11(2)
The Objective Function
13(9)
Explicit Estimation
14(1)
Simple or Unweighted Least Squares (LS) Estimation
15(1)
Weighted Least Squares (WLS) Estimation
15(1)
Generalized Least Squares (GLS) Estimation
15(1)
Maximum Likelihood (ML) Estimation
15(4)
The Determinant Criterion
19(1)
Incorporation of Prior Information About the Parameters
19(1)
Implicit Estimation
19(3)
Parameter Estimation Subject to Constraints
22(1)
Computation of Parameters in Linear Models-Linear Regression
23(26)
The Linear Regression Model
23(3)
The Linear Least Squares Objective Function
26(1)
Linear Least Squares Estimation
27(2)
Polynomial Curve Fitting
29(3)
Statistical Inferences
32(3)
Inference on the Parameters
32(1)
Inference on the Expected Response Variables
33(2)
Solution of Multiple Linear Regression Problems
35(11)
Procedure for Using Microsoft Excel™ for Windows
35(7)
Procedure for Using SigmaPlot™ for Windows
42(4)
Solution of Multiresponse Linear Regression Problems
46(1)
Problems on Linear Regression
46(3)
Vapor Pressure Data for Pyridine and Piperidine
46(1)
Vapor Pressure Data for R142b and R152a
47(2)
Gauss-Newton Method for Algebraic Models
49(18)
Formulation of the Problem
49(1)
The Gauss-Newton Method
50(5)
Bisection Rule
52(1)
Convergence Criteria
52(1)
Formulation of the Solution Steps for the Gauss-Newton Method: Two Consecutive Chemical Reactions
53(2)
Notes on the Gauss-Newton Method
55(1)
Examples
55(9)
Chemical Kinetics: Catalytic Oxidation of 3-Hexanol
55(1)
Biological Oxygen Demand (BOD)
56(1)
Numerical Example 1
57(1)
Chemical Kinetics: Isomerization of Bicyclo [2,1,1] Hexane
58(2)
Enzyme Kinetics
60(1)
Catalytic Reduction of Nitric Oxide
61(1)
Numerical Example 2
62(2)
Solutions
64(3)
Numerical Example 1
65(1)
Numerical Example 2
66(1)
Other Nonlinear Regression Methods for Algebraic Models
67(17)
Gradient Minimization Methods
67(11)
Steepest Descent Method
69(2)
Newton's Method
71(5)
Modified Newton's Method
76(1)
Conjugate Gradient Methods
76(1)
Quasi-Newton or Variable Metric or Secant Methods
77(1)
Direct Search or Derivative Free Methods
78(5)
LJ Optimization Procedure
79(2)
Simplex Method
81(2)
Exercises
83(1)
Gauss-Newton Method for Ordinary Differential Equation (ODE) Models
84(31)
Formulation of the Problem
84(1)
The Gauss-Newton Method
85(7)
Gauss-Newton Algorithm for ODE Models
88(1)
Implementation Guidelines for ODE Models
88(4)
The Gauss-Newton Method-Nonlinear Output Relationship
92(1)
The Gauss-Newton Method-Systems with Unknown Initial Conditions
93(3)
Examples
96(15)
A Homogeneous Gas Phase Reaction
96(2)
Pyrolytic Dehydrogenation of Benzene to Diphenyl and Triphenyl
98(4)
Catalytic Hydrogenation of 3-Hydroxypropanal (HPA) to 1,3-Propanediol (PD)
102(9)
Equivalence of Gauss-Newton with Quasilinearization Method
111(4)
The Quasilinearization Method and its Simplification
111(3)
Equivalence to Gauss-Newton Method
114(1)
Nonlinear Output Relationship
114(1)
Shortcut Estimation Methods for ODE Models
115(18)
ODE Models with Linear Dependence on the Parameters
115(4)
Derivative Approach
116(2)
Integral Approach
118(1)
Generalization to ODE Models with Nonlinear Dependence on the Parameters
119(1)
Estimation of Apparent Rates in Biological Systems
120(9)
Derivative Approach
122(1)
Integral Approach
123(6)
Examples
129(4)
Derivative Approach-Pyrolytic Dehydrogenation of Benzene
129(4)
Practical Guidelines for Algorithm Implementation
133(25)
Inspection of the Data
133(2)
Generation of Initial Guesses
135(4)
Nature and Structure of the Model
135(1)
Asymptotic Behavior of the Model Equations
135(1)
Transformation of the Model Equations
136(2)
Conditionally Linear Systems
138(1)
Direct Search Approach
139(1)
Overstepping
139(2)
An Optimal Step-Size Policy
140(1)
III-Conditioning of Matrix A and Partial Remedies
141(5)
Pseudoinverse
143(1)
Marquardt's Modification
144(1)
Scaling of Matrix A
145(1)
Use of ``Prior'' Information
146(1)
Selection of Weighting Matrix Q in Least Squares Estimation
147(1)
Implementation Guidelines for ODE Models
148(8)
Stiff ODE Models
148(2)
Increasing the Region of Convergence
150(1)
An Optimal Step-Size Policy
150(2)
Use of the Information Index
152(3)
Use of Direct Search Methods
155(1)
Autocorrelation in Dynamic Systems
156(2)
Constrained Parameter Estimation
158(9)
Equality Constraints
158(4)
Lagrange Multipliers
159(3)
Inequality Constraints
162(5)
Optimum Is Internal Point
162(1)
Reparameterization
162(1)
Penalty Function
163(2)
Bisection Rule
165(1)
The Kuhn-Tucker Conditions
165(2)
Gauss-Newton Method for Partial Differential Equation (PDE) Models
167(10)
Formulation of the Problem
167(2)
The Gauss-Newton Method for PDE Models
169(3)
The Gauss-Newton Method for Discretized PDE Models
172(5)
Efficient Computation of the Sensitivity Coefficients
173(4)
Statistical Inferences
177(8)
Inferences on the Parameters
177(2)
Inferences on the Expected Response Variables
179(3)
Model Adequacy Tests
182(3)
Single Response Models
182(2)
Multivariate Models
184(1)
Design of Experiments
185(33)
Preliminary Experimental Design
185(2)
Sequential Experimental Design for Precise Parameter Estimation
187(4)
The Volume Design Criterion
188(1)
The Shape Design Criterion
189(1)
Implementation Steps
190(1)
Sequential Experimental Design for Model Discrimination
191(5)
The Divergence Design Criterion
192(1)
Model Adequacy Tests for Model Discrimination
193(2)
Implementation Steps for Model Discrimination
195(1)
Sequential Experimental Design for ODE Systems
196(6)
Selection of Optimal Sampling Interval and Initial State for Precise Parameter Estimation
196(4)
Selection of Optimal Sampling Interval and Initial State for Model Discrimination
200(1)
Determination of Optimal Inputs for Precise Parameter Estimation and Model Discrimination
200(2)
Examples
202(16)
Consecutive Chemical Reactions
202(5)
Fed-batch Bioreactor
207(6)
Chemostat Growth Kinetics
213(5)
Recursive Parameter Estimation
218(8)
Discrete Input-Output Models
218(1)
Recursive Least Squares (RLS)
219(2)
Recursive Extended Least Squares (RELS)
221(2)
Recursive Generalized Least Squares (RGLS)
223(3)
Parameter Estimation in Nonlinear Thermodynamic Models: Cubic Equations of State
226(42)
Equations of State
226(5)
Cubic Equations of State
227(2)
Estimation of Interaction Parameters
229(1)
Fugacity Expressions Using the Peng-Robinson EoS
230(1)
Fugacity Expressions Using the Trebble-Bishnoi EoS
231(1)
Parameter Estimation Using Binary VLE Data
231(24)
Maximum Likelihood Parameter and State Estimation
232(1)
Explicit Least Squares Estimation
233(1)
Implicit Maximum Likelihood Parameter Estimation
234(2)
Implicit Least Squares Estimation
236(1)
Constrained Least Squares Estimation
236(1)
Simplified Constrained Least Squares Estimation
237(1)
A Potential Problem with Sparse or Not Well Distributed Data
238(2)
Constrained Gauss-Newton Method for Regression of Binary VLE Data
240(2)
A Systematic Approach for Regression of Binary VLE Data
242(2)
Numerical Results
244(1)
The n-Pentane-Acetone System
244(1)
The Methane-Acetone System
245(1)
The Nitrogen-Ethane System
246(1)
The Methane-Methanol System
246(1)
The Carbon Dioxide-Methanol System
246(1)
The Carbon Dioxide-n-Hexane System
247(1)
The Propane-Methanol System
248(2)
The Diethylamine-Water System
250(5)
Parameter Estimation Using the Entire Binary Phase Equilibrium Data
255(6)
The Objective Function
255(2)
Covariance Matrix of the Parameters
257(1)
Numerical Results
258(1)
The Hydrogen Sulfide-Water System
258(1)
The Methane-n-Hexane System
259(2)
Parameter Estimation Using Binary Critical Point Data
261(5)
The Objective Function
261(3)
Numerical Results
264(2)
Problems
266(2)
Data for the Methanol-Isobutane System
266(1)
Data for the Carbon Dioxide-Cyclohexane System
266(2)
Parameter Estimation in Nonlinear Thermodynamic Models: Activity Coefficients
268(17)
Electrolyte Solutions
268(6)
Pitzer's Model Parameters for Aqueous Na2SiO3 Solutions
268(2)
Pitzer's Model Parameters for Aqueous Na2SiO3-NaOH Solutions
270(3)
Numerical Results
273(1)
Non-Electrolyte Solutions
274(5)
The Two-Parameter Wilson Model
276(1)
The Three-Parameter NRTL Model
276(1)
The Two-Parameter UNIQUAC Model
277(1)
Parameter Estimation: The Objective Function
278(1)
Problems
279(6)
Osmotic Coefficients for Aqueous Solutions of KCI Obtained by the Isopiestic Method
279(1)
Osmotic Coefficients for Aqueous Solutions of High-Purity NiCl2
280(1)
The Benzene (1)-i-Propyl Alcohol (2) System
281(1)
Vapor-Liquid Equilibria of Coal-Derived Liquids: Binary Systems with Tetralin
282(1)
Vapor-Liquid Equilibria of Ethylbenzene (1)-o-Xylene (2) at 26.66 kPa
283(2)
Parameter Estimation in Chemical Reaction Kinetic Models
285(37)
Algebraic Equation Models
285(10)
Chemical Kinetics: Catalytic Oxidation of 3-Hexanol
285(2)
Chemical Kinetics: Isomerization of Bicyclo [2,1,1] Hexane
287(1)
Catalytic Reduction of Nitric Oxide
288(7)
Problems with Algebraic Models
295(7)
Catalytic Dehydrogenation of sec-butyl Alcohol
295(2)
Oxidation of Propylene
297(3)
Model Reduction Through Parameter Estimation in the s-Domain
300(2)
Ordinary Differential Equation Models
302(14)
A Homogeneous Gas Phase Reaction
302(1)
Pyrolytic Dehydrogenation of Benzene to Diphenyl and Triphenyl
303(4)
Catalytic Hydrogenation of 3-Hydroxypropanal (HPA) to 1,3-Propanediol (PD)
307(7)
Gas Hydrate Formation Kinetics
314(2)
Problems with ODE Models
316(6)
Toluene Hydrogenation
317(1)
Methylester Hydrogenation
318(2)
Catalytic Hydrogenation of 3-Hydroxypropanal (HPA) to 1,3-Propanediol (PD)-Nonisothermal Data
320(2)
Parameter Estimation in Biochemical Engineering Models
322(31)
Algebraic Equation Models
322(16)
Biological Oxygen Demand
322(1)
Enzyme Kinetics
323(4)
Determination of Mass Transfer Coefficient (kLa) in a Municipal Wastewater Treatment Plant (with PULSAR aerators)
327(3)
Determination of Monoclonal Antibody Productivity in a Dialyzed Chemostat
330(8)
Problems with Algebraic Equation Models
338(6)
Effect of Glucose to Glutamine Ratio on MAb Productivity in a Chemostat
338(2)
Enzyme Inhibition Kinetics
340(1)
Determination of kLa in Bubble-free Bioreactors
341(3)
Ordinary Differential Equation Models
344(3)
Contact Inhibition in Microcarrier Cultures of MRC-5 Cells
344(3)
Problems with ODE Models
347(6)
Vero Cells Grown on Microcarriers (Contact Inhibition)
347(1)
Effect of Temperature on Insect Cell Growth Kinetics
348(5)
Parameter Estimation in Petroleum Engineering
353(38)
Modeling of Drilling Rate Using Canadian Offshore Well Data
353(5)
Application to Canadian Offshore Well Data
355(3)
Modeling of Bitumen Oxidation and Cracking Kinetics Using Data from Alberta Oil Sands
358(13)
Two-Component Models
358(1)
Three-Component Models
359(3)
Four-Component Models
362(2)
Results and Discussion
364(7)
Automatic History Matching in Reservoir Engineering
371(20)
A Fully Implicit, Three Dimensional, Three-Phase Simulator with Automatic History-Matching Capability
371(2)
Application to a Radial Coning Problem (Second SPE Comparative Solution Problem)
373(1)
Matching Reservoir Pressure
373(1)
Matching Water-Oil Ratio, Gas-Oil Ratio or Bottom Hole Pressure
374(1)
Matching All Observed Data
374(2)
A Three-Dimensional, Three-Phase Automatic History-Matching Model: Reliability of Parameter Estimates
376(2)
Implementation and Numerical Results
378(2)
Improved Reservoir Characterization Through Automatic History Matching
380(2)
Incorporation of Prior Information and Constraints on the Parameters
382(2)
Reservoir Characterization Using Automatic History Matching
384(1)
Reliability of Predicted Well Performance Through Automatic History Matching
385(3)
Quantification of Risk
388(1)
Multiple Reservoir Descriptions
388(1)
Case Study-Reliability of a Horizontal Well Performance
389(2)
References 391(12)
Appendix 1 403(7)
A.1.1 The Trebble-Bishnoi Equation of State
403(1)
A.1.2 Derivation of the Fugacity Expression
403(2)
A.1.3 Derivation of the Expression for (∂lnfj/∂xj) T,P,x
405(5)
Appendix 2 410(24)
A.2.1 Listings of Computer Programs
410(1)
A.2.2 Contents of Accompanying CD
411(1)
A.2.3 Computer Program for Example 16.1.2
412(8)
A.2.4 Computer Program for Example 16.3.2
420(14)
Index 434

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