| |
List of Tables |
vi |
| List of Figures |
x |
Section
1
421kb |
Abstract |
xix |
| Objectives and Scope of Work |
xx |
| Executive Summary |
xxii |
| Recommendations For Future Work |
xxvii |
Section
2
632kb |
I |
Introduction |
1 |
| |
|
Overview of Fischer-Tropsch Studies in Bubble Columns |
3 |
| Mass transfer coefficient |
5 |
| Heat transfer coefficient |
6 |
| Gas holdup and bubble size distribution |
6 |
| Flow regime characterization |
10 |
| Effect of solids |
10 |
| Effect of liquid velocity |
11 |
| Overview of Nuclear Density Gauge Studies |
12 |
| Objectives of This Study |
16 |
Section
3
825kb |
II |
Measurement of Gas Holdups By Conventional
Techniques |
17 |
| |
|
Experimental Apparatus and Operating Procedure |
17 |
| Experimental Conditions |
29 |
| Data Acquisition and Reduction Procedures for Gas Holdups
and Solids Concentration Profiles |
29 |
| Average gas holdup - glass columns |
32 |
| Phase fractions - stainless steel columns |
32 |
| Pressure measurements |
32 |
| Solid concentration measurements |
36 |
| Holdup calculations |
42 |
Section
4
1024kb |
Results and Discussion |
47 |
| Description of the flow field |
47 |
| Gas holdup results |
49 |
| Effect of slurry velocity |
51 |
| Effect of solids concentration |
62 |
| Effect of solids type and size |
77 |
Section
5
819kb |
Effect of liquid medium |
82 |
| Effect of distributor type |
85 |
| Effect of column diameter |
87 |
| Physical Properties and Average Gas Holdup Correlations |
92 |
| Physical property measurements |
92 |
| Density measurements |
92 |
| Viscosity measurements |
94 |
| Surface tension measurements |
95 |
| Gas holdup correlations |
97 |
Section
6
1090kb |
III |
Measurement of Phase Fractions By Gamma-Ray
Densitometry |
111 |
| |
|
Theoretical Discussion |
111 |
| Models used to describe three-phase systems |
115 |
| Case I. Perpendicular alignment |
115 |
| Case II. Parallel alignment |
119 |
| Comments on the alignment of the phases |
122 |
| Source Selection and Sensitivity Analysis |
123 |
| Experimental Apparatus and Operating Conditions |
130 |
| Movable assembly mechanism (MAM) |
130 |
| Sources and detectors |
133 |
| Nuclear electronics |
135 |
| Calibration procedures |
141 |
| Data Acquisition and Reduction Procedures |
143 |
Section
7
1013kb |
Gas holdups in two-phase systems |
147 |
| Gas holdups in three-phase systems |
154 |
| Discussion of Results |
154 |
| Independent treatment of all three phases |
155 |
| Two-phase and pseudo two-phase results |
157 |
Section
8
790kb |
IV |
Axial Solids Distribution |
184 |
| |
|
Semi-Infinite Dispersion Model |
184 |
| Summary of Solids Concentration in the Column and Storage
Tank |
188 |
| Results and Discussion |
193 |
Section
9
599kb |
V |
Bubble Size Distributions |
211 |
| |
|
Experimental Techniques for Measurement of the
Disengagement Profile |
215 |
| Theory |
216 |
| Case I. Constant rate disengagement process |
217 |
| Estimating bubble rise velocities and gas holdups during
constant rate disengagement |
223 |
| Data Acquisition and Reduction Procedures |
228 |
Section
10
744kb |
Discussion of Results |
231 |
| Effect of axial position |
247 |
| Effect of column diameter |
249 |
| Comparison of results obtained in the glass and stainless
steel bubble columns |
251 |
Section
11
1117kb |
VI |
Flow Regime Characterization |
256 |
| |
|
Theoretical Background |
256 |
| Discussion of Results |
262 |
| Flow regime transitions based on the MSE |
268 |
| Flow regime transitions based on the PSD |
279 |
Section
12
489kb |
VII |
Nomenclature |
294 |
|
VIII |
Literature Cited |
300 |
|
IX |
Acknowledgements |
311 |