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9780521019842

Parametric Sensitivity in Chemical Systems

by
  • ISBN13:

    9780521019842

  • ISBN10:

    0521019842

  • Format: Paperback
  • Copyright: 2005-09-15
  • Publisher: Cambridge University Press

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Summary

The behavior of a chemical system is affected by many physicochemical parameters. The sensitivity of the system's behavior to changes in parameters is known as parametric sensitivity. When a system operates in a parametrically sensitive region, its performance becomes unreliable and changes sharply with small variations in parameters. Thus, it would be of great value to predict sensitivity behavior in chemical systems. This book is the first to provide a thorough treatment of the concept of parametric sensitivity and the mathematical tool it generated, sensitivity analysis. The emphasis is on applications to real situations. The book begins with definitions of various sensitivity indices and describes the numerical techniques used for their evaluation. Extensively illustrated chapters discuss sensitivity analysis in a variety of chemical reactors - batch, tubular, continuous-flow, fixed-bed - and in combustion systems, air pollution, and metabolic processes. Chemical engineers, chemists, graduate students, and researchers will welcome this valuable resource.

Table of Contents

Preface xv
Introduction
1(8)
The Concept of Sensitivity
1(4)
Uses of the Sensitivity Concept
5(2)
Overview of the Book Contents
7(2)
References
8(1)
Introduction to Sensitivity Analysis
9(27)
Sensitivity Indices
9(8)
Local Sensitivity
9(2)
Example 2.1 Conversion sensitivity in a batch reactor
11(2)
Objective Sensitivity
13(1)
Example 2.2 Sensitivity of the maximum yield in an isothermal batch reactor with consecutive reactions
14(2)
Global Sensitivity
16(1)
Computation of Sensitivity Indices
17(19)
Local Sensitivity
17(1)
Example 2.3 Sensitivity analysis of an isothermal batch reactor with consecutive reactions of arbitrary order
18(6)
Global Sensitivity
24(8)
Nomenclature
32(1)
References
33(3)
Thermal Explosion in Batch Reactors
36(44)
Basic Equations
37(1)
Geometry-Based Criteria for Thermal Runaway
38(17)
The Case of Negligible Reactant Consumption: Semenov Theory
38(5)
Example 3.1 Application of Semenov criterion to thermal explosion of methyl nitrate
43(1)
Criteria Accounting for Reactant Consumption
44(9)
Example 3.2 Application of AE and VF criteria to thermal explosion of methyl nitrate
53(2)
Sensitivity-Based Criteria for Thermal Runaway
55(15)
The Morbidelli and Varma (MV) Criterion
56(7)
Example 3.3 Application of the MV criterion to catalytic hydrolysis of acetic anhydride
63(1)
The Vajda and Rabitz (VR) Criterion
64(3)
Example 3.4 A comparison between various criteria in predicting explosion limits in azomethane decomposition
67(2)
The Strozzi and Zaldivar (SZ) Criterion
69(1)
Explicit Criteria for Thermal Runaway
70(10)
Nomenclature
76(1)
References
77(3)
Runaway in Tubular Reactors
80(63)
Basic Equations for Tubular Plug-Flow Reactors
81(2)
Plug-Flow Reactors with Constant External Cooling
83(18)
Runaway Criteria
83(2)
Example 4.1 Runaway behavior in the naphthalene oxidation reactor
85(4)
The Region of Pseudo-Adiabatic Operation (PAO)
89(5)
Influence of PAO on the Runaway Region
94(6)
Example 4.2 Runaway behavior in a naphthalene oxidation reactor operating in the pseudo-adiabatic operation region
100(1)
Plug-Flow Reactors Varying Coolant Temperature
101(10)
The Regions of Pseudo-Adiabatic Operation
101(3)
Influence of PAO on Runaway Regions
104(7)
Role of Radial Temperature and Concentration Gradients
111(5)
Complex Kinetic Schemes
116(27)
The Case of Two Consecutive Reactions (A → B → C)
119(11)
Example 4.3 Reactor operation diagram for naphthalene oxidation process
130(2)
The Case of Two Parallel Reactions (A → B → C)
132(3)
Example 4.4 Reactor operation diagram for ethylene epoxidation process
135(3)
Nomenclature
138(2)
References
140(3)
Parametric Sensitivity in Continuous-Flow Stirred Tank Reactors
143(26)
Sensitivity Analysis
144(8)
Regions of Parametrically Sensitive Behavior
152(7)
Role of the Involved Physicochemical Parameters
152(5)
Relation between Multiplicity and Sensitivity Behavior
157(2)
Role of Mixing on Reactor Parametric Sensitivity
159(4)
Explicit Criteria for Parametric Sensitivity
163(6)
Nomenclature
166(1)
References
167(2)
Runaway in Fixed-Bed Catalytic Reactors
169(51)
The Heterogeneous Model of a Fixed-Bed Catalytic Reactor
170(2)
Runaway of a Single Catalyst Particle: Local Runaway
172(17)
Critical Conditions for Local Runaway of Particle Temperature
173(6)
Runaway Regions
179(10)
Runaway of Fixed-Bed Reactors: Global Runaway
189(24)
Critical Conditions for Global Runaway of Particle Temperature
189(3)
Runaway Regions
192(4)
Example 6.1 Experimental analysis of runaway in a fixed-bed reactor for vinyl acetate synthesis
196(7)
Example 6.2 Experimental analysis of runaway in a fixed-bed reactor for carbon monoxide oxidation
203(2)
Limiting Behavior
205(1)
Example 6.3 Runaway regions in the case of severe intraparticle mass transfer resistance
206(2)
Effect of Pseudo-Adiabatic Operation on Runaway Regions
208(5)
Explicit Criteria for Runaway
213(7)
Nomenclature
216(2)
References
218(2)
Parametric Sensitivity and Ignition Phenomena in Combustion Systems
220(27)
General Definition of Ignition Limits
221(3)
Explosion Limits in Hydrogen-Oxygen Mixtures
224(10)
Application of the Sensitivity Criterion
224(7)
Comparison between Experimental and Calculated Explosion Limits
231(3)
Further Insight into Explosion Behavior in Hydrogen-Oxygen Mixtures
234(13)
Explosion in the Low Pressure Region
235(8)
Explosion in the High Pressure Region
243(1)
References
244(3)
Sensitivity Analysis in Mechanistic Study and Model Reduction
247(40)
Sensitivity Analysis in Mechanistic Studies
248(25)
Applications of the Green's Function Method
249(1)
Example 8.1 Oxidation of wet carbon monoxide
250(4)
Example 8.2 Sensitivity analysis of the Belousov-Zhabotinsky oscillating reaction
254(5)
Applications of the Finite Difference Method
259(1)
Example 8.3 Explosion mechanism in hydrogen-oxygen systems: The first limit
260(5)
Example 8.4 Explosion mechanism in hydrogen-oxygen systems: The second limit
265(4)
Example 8.5 Explosion mechanism in hydrogen-oxygen systems: The third limit
269(2)
Example 8.6 Explosion mechanism in hydrogen-oxygen systems: The weak-strong explosion boundaries (WSEB)
271(2)
Reduction of Detailed Kinetic Models
273(14)
Example 8.7 Minimum reduced kinetic model for the explosion limits of hydrogen-oxygen systems
274(6)
Example 8.8 Reduced kinetic model for the combustion of methane-ethane systems
280(4)
References
284(3)
Sensitivity Analysis in Air Pollution
287(25)
Basic Equations
288(2)
Sensitivity Analysis of Regional Air Quality with Respect to Emission Sources
290(12)
Definition of Sensitivities
290(2)
A Case Study: Emissions of NOx and SO2 in the Eastern United States
292(10)
Global Sensitivity Analysis of Trajectory Model for Photochemical Air Pollution
302(10)
Global Sensitivities and the FAST Method
302(1)
A Case Study: Emissions of NO, NO2, Reactive Hydrocarbons and O3
303(7)
References
310(2)
Sensitivity Analysis in Metabolic Processes
312(23)
The General Approach for Sensitivity Analysis
313(7)
Mathematical Framework
313(4)
A Case Study: The Yeast Glycolytic Pathway
317(3)
The Matrix Method from Metabolic Control Theory
320(15)
Model Framework
322(2)
A Case Study: The Metabolic Pathway of Gluconeogenesis from Lactate
324(4)
Some Useful Theorems for Sensitivity Analysis
328(2)
Nomenclature
330(1)
References
331(4)
Author Index 335(4)
Subject Index 339

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