|
Acknowledgement |
iii |
List of Tables |
vi |
List of Figures |
vii |
List of Symbols |
xii |
Abstract |
xv |
Section 1
867kb |
I |
Introduction |
1.1 |
II |
Descriptions of Hydrodynamic Models |
2.1 |
|
2.1
|
Introduction
|
2.1
|
2.2
|
Hydrodynamic Models
|
2.1
|
2.3
|
Constitutive Equations
|
2.3
|
2.4
|
Solid Viscosity From Kinetic Theory Approach
|
2.6
|
2.5
|
Reaction and Mass Transfer
|
2.8
|
2.6
|
Species Balances
|
2.8
|
III |
Gas Holdup of Gas-Liquid Fluidization |
3.1 |
|
3.1
|
Introduction
|
3.1
|
3.2
|
Hydrodynamic Models
|
3.2
|
3.3
|
Operating Conditions
|
3.4
|
3.4
|
Numerical Considerations
|
3.5
|
3.5
|
Results and Discussions
|
3.8
|
Section 2
1271kb |
IV |
Methanol Synthesis With Slurry
Circulation |
4.1 |
|
4.1
|
Introduction
|
4.1
|
4.2
|
Reaction Kinetics and Mass Transfer
|
4.1
|
4.3
|
Species Balance
|
4.3
|
4.4
|
Mathematical Models (Empirical)
|
4.3
|
4.5
|
Operation Conditions
|
4.5
|
4.6
|
Numerical Considerations
|
4.6
|
4.7
|
Computational Results and Discussions
|
4.9
|
Section 3
3213kb |
V |
Methanol Synthesis Without Slurry
Circulation |
5.1 |
|
5.1
|
Introduction
|
5.1
|
5.2
|
Reaction and Kinetic Model
|
5.1
|
5.3
|
Mathematics Model (Kinetic Theory)
|
5.2
|
5.4
|
Operation Conditions
|
5.6
|
5.5
|
Numerical Considerations
|
5.8
|
5.6
|
Computational Results and Discussions
|
5.11
|
5.7
|
Convergence Check
|
5.20
|
VI |
Separation of Pyrite From Coal in an
Inclined Electro-Fluidized Bed |
6.1 |
|
6.1
|
Introduction
|
6.1
|
6.2
|
Hydrodynamic Model
|
6.4
|
6.3
|
Operation Conditions
|
6.7
|
6.4
|
Numerical Considerations
|
6.7
|
6.5
|
Computational Results and Discussions
|
6.12
|
VII |
Summary and Recommendations |
7.1 |
|
Appendix
|
|
A |
Numerical Basis of Program MFREK
885kb |
A.1 |
B |
Organization and User Menu of MFREK
884kb |
B.1 |
C |
Source Fortan Code of MFREK and a Sample Input Data
2311kb |
C.1 |
Bibliography
344kb |
D.1 |