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 15. Integral 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.

Like Unit 14, Unit 15 considers the situation where the model for a set of kinetics experiments takes the form of a differential equation. This happens when kinetics data for a single reaction are generated using either a batch reactor or a plug flow reactor. In Unit 15, the differential equation is first solved analytically to obtain an algebraic equation. At that point, the fitting process again becomes the same as that described for a CSTR in Unit 13. This integral data analysis approach is generally more accurate and therefore preferred for the analysis of kinetics data from batch reactors and PFRs.

Learning Resources

Teaching Resources

Practice Problems

1. Repeat any problem from Unit 14 using an integral data analysis.

2. Suppose you are studying the kinetics of the gas phase condensation, reaction (2a), using a 600 cm3 perfectly mixed batch reactor. In one experiment you charged the reactor with 2.3 atm of A and 2.0 atm of B (no Z was initially present) at 300 K and then recorded the total pressure as a function of time. The resulting data are presented in this Table (.xlsx file). For this one set of experimental data, does the rate expression given in equation (2b) provide an adequate description of the reaction kinetics? If so, what is the best value for the rate coefficient, and what is the uncertainty in that value?

  A + B → Z (2a)  
  r1 = k1PAPB (2b)  

(Problem Statement as .pdf file)

3. Suppose you are studying gas phase reaction (3a) using a laboratory PFR with an inside diameter of 2.2 cm and a length of 30 cm. The reactor operates isothermally, at steady state and at constant pressure. A series of experimental runs were made at 723 K using different combinations of feed flow rate and reactor pressure. In each run, the feed consisted of pure A and the mole fraction of A was measured at the reactor outlet. The experimental data are presented in this Table (.xlsx file). Determine whether the reaction rate can be accurately modeled using the rate expression given in equation (3b), and if it can, compute the best value for the rate coefficient along with its uncertainty.

  A → Y + Z (3a)  
  r1 = k1PA (3b)  

(Problem Statement as .pdf file)

4. Suppose that the liquid-phase Diels-Alder combination of cyclopentadiene (A) and benzoquinone (B), reaction (4a), was studied in the liquid phase using a 2 gal perfectly mixed batch reactor. The temperature was constant and the same in all of the experiments. In any one experiment the reactor was charged with known concentrations of A and B and the concentration of A was measured after a known reaction time. Using the resulting data, in this Excel© file, determine whether the rate expression in equation (4b) accurately predicts the reaction kinetics. If it does, determine the best value for the rate coefficients, including 95% confidence limits.

  A + B → Y (4a)  
  r3a=k3aCACB (4b)  

(Problem Statement as .pdf file)

5. Suppose that the gas phase decomposition of A, reaction (5a), was studied in an isothermal, isobaric, steady-state PFR. In every experiment the temperature was 675 K, the pressure was 1 atm, and the feed was pure A, an ideal gas. The space time was varied from one experiment to the next, and the fractional conversion of A was measured. Using the resulting data, in this Excel© file, determine whether the rate expression in equation (5b) accurately predicts the reaction kinetics. If it does, determine the best value for the rate coefficient, including 95% confidence limits.

  A → Y + Z (5a)  
  r4a=k4aCA (5b)  

(Problem Statement as .pdf file)