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 5. Empirical and Theoretical Rate Expressions

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.

This first section of Part II of the course focuses upon the selection of an equation to be tested as a rate expression. The equation to be tested can be chosen simply for its mathematical convenience. Alternatively, theory can be used to select the mathematical form of the equation to be tested. For some reactions, theory can be applied directly. In other cases the reaction must be described in terms of a group of reactions that comprise what is known as a reaction mechanism. In the latter case theory can be applied to the reactions in the mechanism which are then combined to get the mathematical form of the equation to be tested.

Unit 5 takes a closer look at rate expressions, starting with a common empirical form for a rate expression known as a power-law rate expression. It then defines an elementary reaction and presents two theories that allow the prediction of the mathematical form of the rate expression for an elementary reaction. Those theories are called the Collision Theory and the Transition State Theory.

Learning Resources

Teaching Resources

  • Archive (.zip) - Contains all teaching resources listed below for this unit
  • Sample Class
  • Alternative Questions (.pdf) that could be used in a pre-class quiz
  • Alternative In-Class Learning Activities
    • Alternative Activity 5.1 (.zip) - an activity where students explore the shape of plots of rate versus conversion for various empirical rate expressions.
    • Alternative Activity 5.2 (.zip) - an activity where students analyze different chemical reactions and determine whether they could be elementary reactions.

Practice Problems

1. Suppose that for a quick preliminary calculation you need an approximate value for the rate of reaction (1a) below for a mixture containing 46% H2, 31% CO2, 22% CO, and 1% CH3OH at a total pressure of 49.3 atm and a temperature of 327 °C. Suppose further that you have obtained an old company report which says that the rate expression given in equation (1b) below was shown to fit experimental data from reaction (1a) at similar compositions and pressures, but at the temperatures given in the table below. Using the data in that table, what is your best estimate for the rate of reaction (1a) at the conditions of interest to you. (Note: the rate expression used in this example is made up and should not be used for any purpose other than answering this question.)

  CO + 2 H2 ↔ CH3OH (1a)  
  r1a = k1a⋅PCO0.46 ⋅PH21.37 (1b)  

 

  Temperature k1  
  (°C) (mol min-1 L-1 atm-1.83)  
  ---------- --------------------  
  80 0.024  
  110 0.138  
  140 0.606  
  170 2.18  

(Problem Statement as .pdf file)

2. Collision theory can't be applied directly to a unimolecular reaction like that given in equation (2a) below. One approach to developing a theory for unimolecular reactions is to assume that the reactant molecule must first undergo a collision that results in it gaining internal energy. Collision theory can be used to estimate the rate of this preliminary step. Assuming a system contains pure ethane (collision diameter equal to 0.53 nm) at atmospheric pressure and 300 °C, estimate the corresponding pre-exponential factor.

  C2H6 → 2 CH3 (2a)  

(Problem Statement as .pdf file)

3. Consider the reaction between a diatomic molecule and an atom where the activated complex is non-linear. Use transition state theory to write out an expression that explicitly shows all the places that temperature appears in the rate coefficient. You may leave your answer in terms of masses, moments of inertia, vibrational frequencies, etc. of relevant species, but you must expand all summations and continuous products. Determine how many times the temperature appears.

(Problem Statement as .pdf file)

4. According to simple collision theory the rate coefficient for reaction (4a) will depend upon temperature according to equation (4b). Using the rate coefficient data in the table below (and this Excel file), determine whether this is true, and, if it is, find the best values of the pre-exponential factor and the activation energy.

  2 A → Y + Z (4a)  
  k1 =k0,1T0.5exp(-E1/RT) (4b)  

 

  T (°C) k (L mol-1 min-1)  
  10 2.63 x 10-4  
  22 4.78 x 10-4  
  40 1.52 x 10-3  
  54 4.18 x 10-3  
  65 9.07 x 10-3  
  78 2.14 x 10-2  
  89 4.20 x 10-2  
  103 9.42 x 10-2  

(Problem Statement as .pdf file)