CONTENTS

Front Matter

Title Page, Preface and Acknowledgements
About the Author
Status, History, Issues and Updates
Complementary Textbooks
Teaching Notes and Resources
A Note about Numerical Solutions

Course Units

I. Chemical Reactions
1. Stoichiometry and Reaction Progress
2. Reaction Thermochemistry
3. Reaction Equilibrium
II. Chemical Reaction Kinetics
A. Rate Expressions
4. Reaction Rates and Temperature Effects
5. Empirical and Theoretical Rate Expressions
6. Reaction Mechanisms
7. The Steady State Approximation
8. Rate-Determining Step
9. Homogeneous and Enzymatic Catalysis
10. Heterogeneous Catalysis
B. Kinetics Experiments
11. Laboratory Reactors
12. Performing Kinetics Experiments
C. Analysis of Kinetics Data
13. CSTR Data Analysis
14. Differential Data Analysis
15. Integral Data Analysis
16. Numerical Data Analysis
III. Chemical Reaction Engineering
A. Ideal Reactors
17. Reactor Models and Reaction Types
B. Perfectly Mixed Batch Reactors
18. Reaction Engineering of Batch Reactors
19. Analysis of Batch Reactors
20. Optimization of Batch Reactor Processes
C. Continuous Flow Stirred Tank Reactors
21. Reaction Engineering of CSTRs
22. Analysis of Steady State CSTRs
23. Analysis of Transient CSTRs
24. Multiple Steady States in CSTRs
D. Plug Flow Reactors
25. Reaction Engineering of PFRs
26. Analysis of Steady State PFRs
27. Analysis of Transient PFRs
E. Matching Reactors to Reactions
28. Choosing a Reactor Type
29. Multiple Reactor Networks
30. Thermal Back-Mixing in a PFR
31. Back-Mixing in a PFR via Recycle
32. Ideal Semi-Batch Reactors
IV. Non-Ideal Reactions and Reactors
A. Alternatives to the Ideal Reactor Models
33. Axial Dispersion Model
34. 2-D and 3-D Tubular Reactor Models
35. Zoned Reactor Models
36. Segregated Flow Models
37. Overview of Multi-Phase Reactors
B. Coupled Chemical and Physical Kinetics
38. Heterogeneous Catalytic Reactions
39. Gas-Liquid Reactions
40. Gas-Solid Reactions

Supplemental Units

S1. Identifying Independent Reactions
S2. Solving Non-differential Equations
S3. Fitting Linear Models to Data
S4. Numerically Fitting Models to Data
S5. Solving Initial Value Differential Equations
S6. Solving Boundary Value Differential Equations

Unit 13. CSTR Data Analysis

This website provides learning and teaching tools for a first course on kinetics and reaction engineering. The course is divided into four parts (I through IV). Here, in Part II of the course, the focus is on chemical reaction kinetics, and more specifically, on rate expressions, which are mathematical models of reaction rates. As you progress through Part II, you will learn how rate expressions are generated from experimental kinetics data.

Part II of the course concludes with Section C which describes how to test a rate expression (Section A) using experimental data (Section B). The testing of a rate expression entails its substitution into the model for the experimental reactor and the subsequent fitting of that model to the experimental data. The end result will reveal whether the selected rate expression offers a sufficiently accurate representation of the rate of the reaction under consideration. If it does, the fitting process also will yield the best values for the parameters that appear in the selected rate expression.

Unit 13 describes the analysis of kinetics data that have been generated using an isothermal, steady state CSTR. When only one reaction takes place in the reactor, the model for any one experiment in an isothermal, steady state CSTR is an algebraic equation. In this unit, the model equation is re-written in the form of a linear equation (if necessary), linear least squares is used to fit the resulting linear model to the data, the accuracy of the fitted model is assessed, and if the accuracy is acceptable, the kinetic parameters and their uncertainties are calculated from the slope(s) and intercept of the linear model that was fit to the data.

Learning Resources

Teaching Resources

Practice Problems

1. Suppose you wish to test equation (1a) to determine whether it is satisfactory as a rate expression for liquid phase reaction (1b). To do so you used a 3 gal. reactor that had been tested and shown to behave as an ideal CSTR. You made 15 steady state experimental runs using the inlet flow rates and compositions shown in this Table (.xlsx file), and in each run you recorded the steady state conversion, also shown in the table. Determine whether equation (1a) is an acceptable rate expression, and if it is, estimate the values and uncertainties for the two rate coefficients.

  r1b = kf⋅CA2 - kr⋅CY⋅CZ (1a)  
  A ↔ Y + Z (1b)  

(Problem Statement as .pdf file)

2. Suppose that the liquid-phase decomposition of isobutyl iodide (1-Iodo-3-methylpropane) according to reaction (2a) was studied in hexachlorobutadiene solution using a CSTR. At the temperature studied, 160 °C, the reaction is effectively irreversible. In a series of experiments using a feed containing iodine and isobutyl iodide in varying concentrations, the space time was varied and the steady state conversion of isobutyl iodide was measured. Using the resulting data in this Excel© file, determine whether the rate expression in equation (2b) accurately predicts the reaction kinetics. If it does, determine the best value for the rate coefficient, including 95% confidence limits.

  2 (CH3)2CHCH2I → (CH3)3CH + (CH3)2C=CH2 + I2 (2a)  
  r2a = k2aC(CH3)2CHCH2I(CI2)0.5 (2b)  

(Problem Statement as .pdf file)