Acknowledgement |
v |
Abstract |
vii |
1 |
Introduction
403kb |
1 |
|
1.1 |
Motivation for the Thesis |
1 |
|
1.1.1 |
Importance of bubble column reactors |
1 |
1.1.2 |
The importance of reactor modeling |
6 |
1.1.3 |
The need for determining model parameters |
7 |
1.2 |
Problem Formulation |
9 |
|
1.2.1 |
Overview |
9 |
1.2.2 |
Coalescence and breakup rates |
10 |
1.2.3 |
Liquid circulation |
12 |
1.2.4 |
Dynamic gas disengagement |
13 |
2 |
Experimental
479kb |
15 |
|
2.1 |
Experimental Apparatus |
15 |
2.2 |
Measurement Principle |
17 |
|
2.2.1 |
The five-point probe of Burgess and Calderbank |
17 |
2.2.2 |
The five-point probe of Steinemann and Buchholz |
19 |
2.3 |
Estimation of the Bubble Parameters |
20 |
|
2.3.1 |
Technique of Burgess and Calderbank |
20 |
2.3.2 |
Technique of Steinemann and Buchholz |
22 |
2.4 |
Experimental Results |
23 |
2.5 |
Conclusion |
31 |
3 |
Coalescence and Breakup
962kb |
33 |
|
3.1 |
Introduction |
33 |
3.2 |
Binary Bubble Coalescence |
37 |
|
3.2.1 |
Binary bubble collision frequency |
38 |
3.2.2 |
Coalescence efficiency |
40 |
3.3 |
Model for Bubble Breakup |
43 |
|
3.3.1 |
Arrival or bombarding frequency of eddies |
44 |
3.3.2 |
Breakage probability (efficiency) |
46 |
3.3.3 |
The expression for breakage rate |
49 |
3.3.4 |
Breakage kernel or breakage size distribution |
50 |
3.4 |
Results and Discussion |
52 |
|
3.4.1 |
Coalescence efficiency |
52 |
3.4.2 |
Specific coalescence rate |
54 |
3.4.3 |
Breakage kernel |
58 |
3.4.4 |
Specific breakage rate |
61 |
3.5 |
Conclusion |
62 |
4 |
Approach of Two Fluid Particles
824kb |
65 |
|
4.1 |
Introduction |
66 |
4.2 |
Simple Parallel-Film Model |
67 |
|
4.2.1 |
Expression of film area |
67 |
4.2.2 |
Expression for interaction time |
72 |
4.2.3 |
Virtual mass coefficient |
73 |
4.3 |
General Parallel-Film Model |
75 |
4.4 |
Results and Discussion |
80 |
|
4.4.1 |
Zero external force |
80 |
4.4.2 |
Effect of external forces |
85 |
4.4.3 |
Effect of virtual mass |
87 |
4.4.4 |
Comparison with experimental data |
88 |
4.5 |
Conclusion |
92 |
5 |
Local Bubble Size Distribution
521kb |
95 |
|
5.1 |
Introduction |
95 |
5.2 |
Population Balance Model |
97 |
|
5.2.1 |
Equations of balance |
97 |
5.2.2 |
Viscous and buoyancy coalescence |
101 |
5.2.3 |
Energy dissipation rate |
103 |
5.2.4 |
Boundary conditions |
104 |
5.3 |
Results and Discussion |
105 |
5.4 |
Conclusion |
110 |
6 |
Liquid Circulation
1157kb |
113 |
|
6.1 |
Introduction |
113 |
6.2 |
Pseudo-Homogeneous Fluid Model |
117 |
|
6.2.1 |
Equation of motion |
124 |
6.2.2 |
Expression of liquid velocity |
121 |
6.3 |
Two-Fluid Model |
124 |
|
6.3.1 |
Equation of motion |
124 |
6.3.2 |
Expression of liquid velocity |
127 |
6.4 |
Results and Discussion |
129 |
|
6.4.1 |
Pseudo-homogeneous model |
129 |
6.4.2 |
Two-fluid model |
138 |
6.5 |
Conclusion |
144 |
7 |
Dynamic Gas Disengagement
1078kb |
147 |
|
7.1 |
Introduction |
147 |
7.2 |
Experimental Technique and Data Treatment |
151 |
7.3 |
Holdup Structure and Rise Velocities |
154 |
7.4 |
Non-Uniform Distribution |
159 |
7.5 |
Bubble Size and Specific Interfacial Area |
160 |
7.6 |
Results and Discussion |
162 |
|
7.6.1 |
Bubble size and interfacial area |
162 |
7.6.2 |
Non-uniform distribution |
169 |
7.7 |
Conclusion |
171 |
8 |
Conclusions and Recommendations
422kb |
173 |
|
8.1 |
Conclusions |
173 |
8.2 |
Recommendations |
175 |
Nomenclature |
177 |
Bibliography
380kb |
185 |