Section 1
326kb |
I |
Introduction |
1 |
II |
Literature
Review |
3 |
|
A |
Gas Flow in Bubble Columns |
3 |
B |
Fischer-Tropsch Derived Waxes |
3 |
|
1 |
Effect of Temperature |
5 |
2 |
Effect of Solids |
7 |
3 |
Effect of Pressure and Gas Type |
7 |
4 |
Effect of Superficial Gas Velocity on Flow Regimes |
8 |
5 |
Effect of Column Diameter |
9 |
6 |
Effect of Liquid Medium |
10 |
7 |
Effect of Static Liquid Height |
10 |
8 |
Effect of Distributor Type |
11 |
C |
Non-Wax Liquid Mediums |
12 |
D |
Thesis Objectives and Motivation |
16 |
Section 2
507kb |
III |
Experiment |
18 |
|
A |
Experimental Apparatus |
18 |
|
1 |
Apparatus Description |
18 |
2 |
Operation |
21 |
B |
Measurements of Average Gas Hold-up |
21 |
|
1 |
Hot-Flow Runs |
22 |
2 |
Cold-Flow Runs |
23 |
C |
Measurements of Physical Properties |
23 |
|
1 |
Fischer Tropsch Derived Waxes |
23 |
2 |
Aqueous Mixtures |
33 |
D |
Effects of Butanol and CMC on Physical
Properties |
37 |
Section 3
995kb |
IV |
Average
Gas Hold Up |
42 |
|
A |
Fischer-Tropsch Derived Waxes |
42 |
|
1 |
Reproducibility and Effect of Operating Procedure |
42 |
2 |
Effect of Temperature |
45 |
3 |
Effect of Column Diameter |
51 |
4 |
Effect of Distributor Type |
53 |
B |
Pure Liquids |
56 |
|
1 |
Effect of Start-up Procedure |
67 |
2 |
Effect of Column Diameter |
58 |
3 |
Effect of Distributor Type |
61 |
4 |
Effect of Liquid Medium |
61 |
C |
Aqueous Solutions of n-Butanol |
65 |
|
1 |
Effect of n-Butanol Concentration |
65 |
2 |
Effect of Start-up Procedure |
67 |
3 |
Effect of Column Diameter |
67 |
4 |
Effect of Distributor Type |
70 |
5 |
Comparison With Other Foaming Mediums |
75 |
D |
Aqueous Solutions of n-Butanol With CMC |
75 |
|
1 |
Effect of CMC Concentration |
75 |
2 |
Effect of Column Diameter |
80 |
3 |
Effect of Distributor Type |
83 |
4 |
Effect of Viscosity on Gas Hold-up |
85 |
Section 4
575kb |
V |
Bubble
Dynamics |
90 |
|
A |
Data Acquisition |
90 |
B |
Procedure for Obtaining Bubble Sizes |
92 |
|
1 |
Fischer Tropsch Derived Waxes |
93 |
2 |
Pure Liquids |
94 |
3 |
Aqueous Solutions of Butanol With CMC |
94 |
VI |
Sauter Mean Bubble Diameter |
101 |
|
A |
FT Derived Waxes |
101 |
|
1 |
Effect of Operating Temperature |
101 |
2 |
Effect of Distributor Type |
103 |
3 |
Effect of Wax Type |
103 |
B |
Pure Liquids |
106 |
|
1 |
Effect of Distributor Type |
106 |
C |
Aqueous Solutions of n-Butanol |
106 |
|
1 |
Effect of Distributor Type |
106 |
D |
Aqueous Solutions of n-Butanol With CMC |
110 |
|
1 |
Effect of Distributor Type |
110 |
2 |
Effect of Column Diameter |
112 |
3 |
Effect of Physical Properties |
114 |
Section 5
580kb |
VII |
Correlations |
116 |
|
A |
FT Derived Waxes |
116 |
|
1 |
Average Gas Hold-up |
116 |
2 |
Specific Gas-Liquid Interfacial Area |
118 |
B |
Pure Liquids |
121 |
|
1 |
Average Gas Hold-up |
121 |
2 |
Specific Gas-Liquid Interfacial Area |
125 |
C |
Aqueous Solutions of n-Butanol |
129 |
|
1 |
Average Gas Hold-up |
129 |
2 |
Specific Gas-Liquid Interfacial Area |
132 |
D |
Aqueous Solutions of n-Butanol With CMC |
134 |
|
1 |
Average Gas Hold-up |
134 |
Section 6
765kb |
VIII |
Conclusions and Recommendations |
141 |
Notations |
141 |
Literature Cited |
144 |
Appendices |
|
A |
Summary of Runs with FT Derived Waxes |
150 |
Section 7
812kb |
B |
Summary of DGD Results for Runs with FT
Derived Waxes |
173 |
C |
Summary of Runs with Non-Wax Liquid
Mediums |
178 |
D |
Summary of DGD Results for Runs With Non-Wax
Liquid Mediums |
193 |
E |
Procedures for Measuring Physical Properties
of Non-Wax Liquid Mediums |
206 |
F |
Dynamic Gas Disengagement Technique |
213 |
Vita |
227 |