|
Abstract |
Section
1
1459kb |
I |
Introduction |
4 |
II |
Objectives and Scope of Present Work |
6 |
|
Task 1: Model Validation |
6 |
Task 2: Bubble Dynamics Studies |
6 |
Task 3: Gas/Liquid Mixing |
7 |
|
Gas Mixing |
7 |
Liquid Mixing |
7 |
Catalyst Mixing |
7 |
Task 4: Model Implementation |
7 |
III |
Amoco Cold-Flow Experiments: Bed Expansion and Phase
Holdups |
7 |
|
Equipment and Procedures |
8 |
Experimental Conditions and Data Collection |
9 |
Data Analysis and Results |
9 |
|
Phase Holdup and Other Hydrodynamic Parameters |
9 |
Catalyst Bed Expansion |
11 |
IV |
Amoco Cold-Flow Experiments: Radial Uniformity of Phase
Holdups |
12 |
|
Review of Prior Work |
12 |
Equipment and Procedure |
13 |
Experimental Conditions and Data Collection |
13 |
Data Analysis |
14 |
Results and Discussion |
14 |
V |
Amoco Cold-Flow Experiments: Axial Slurry Dispersion |
15 |
|
Background |
15 |
Review of Liquid Dispersion in Multi-Phase Fluidization |
16 |
|
Gas/Liquid Systems |
16 |
Gas/Slurry Systems |
17 |
Gas/Slurry/Solid System |
18 |
Reacting Systems |
18 |
Tracer Selection |
19 |
Bench-Scale Experiments and Results |
20 |
|
Du Pont Stadis-450 |
20 |
Mobay Blue ZV Dye |
21 |
Thiophene |
21 |
Pilot Plant Testing of Thiophene as a Tracer |
21 |
Equipment |
22 |
Pilot Plant Results and Discussion |
23 |
|
Data Collection |
23 |
Data Analysis |
24 |
Conclusions |
26 |
Section
2
1533kb |
VI |
Bubble Dynamics |
26 |
|
Experimental System |
27 |
|
Description of the Apparatus |
27 |
Fluids and Solids |
28 |
Bed Expansion and Pressure-Drop Measurements |
28 |
|
Bed Expansion Measurements |
28 |
Pressure-Drop Measurements |
28 |
Light Beam Probe and Bubble Breakup Model |
29 |
|
Description of the Light Beam Probe |
29 |
Results of the Light Beam Technique |
29 |
Equilibrium Bubble Size Model |
29 |
Bubble Breakup and the Critical Particle Size |
30 |
Holography |
30 |
|
Description of Holographic Technique |
30 |
Holographic Analysis System |
31 |
Results |
31 |
Resistivity Probe |
31 |
Summary |
32 |
Recommendations |
32 |
VII |
Hydrocarbon Research, Incorporated, PDU Experiments |
33 |
|
Samples and Data Collection |
33 |
|
PDU Operating Conditions |
33 |
Liquid Samples |
33 |
PDU Reactor Effluent Composition |
33 |
Catalyst Samples |
33 |
Gamma-Ray Scan |
34 |
Density and Viscosity of PDU Reactor Liquid Slurry Samples |
35 |
Data Transformations |
37 |
|
Gas Velocity |
37 |
Slurry Velocity |
37 |
Catalyst Bed Expansions |
38 |
Phase Volume Fractions |
39 |
|
Mass Absorption Coefficients for the PDU Fluid Dynamics
Tests |
40 |
Volume Fractions |
40 |
Discussion |
41 |
Comparison with Cold-Flow Pilot Plant Tests |
42 |
VIII |
Mathematical Model |
43 |
|
Review of the Bhatia-Epstein Model |
44 |
Model Parameters |
45 |
Cold-Flow Tests |
46 |
Application to HRI PDU-10 Tests |
48 |
Comparison of PDU and Cold-Flow Pilot Plant Model Results |
50 |
Section
3
403kb |
IX |
Model Applications |
50 |
X |
Conclusions |
51 |
Acknowledgements |
52 |
References |
53 |
Nomenclature |
58 |
Tables 1096kb |
60-113 |
Figures 1595kb |
114-206 |
Appendix A: Catalyst Bed Expansions and Phase
Holdups for Runs 218-224 |
207 |
Appendix B: Liquid Dispersion Data Analysis |
235 |
Appendix C: Viscosity and Density of H-Coal PDU
Liquid Slurry Samples: Battelle Institute Final Report |
245 |
Appendix D: Viscosity and Density of H-Coal PDU
Liquid Slurry Samples: Oak Ridge National Laboratories Final Report |
258 |
Appendix E: Calculation: Force to Suspend a
Catalyst Particle |
280 |
Appendix F: I/IO Data For PDU-10 Fluid Dynamic Tests |
284 |
Appendix G: Prediction of Richardson-Zaki Parameters
For PDU Experimental Modeling |
301 |