| Foreward |
iii |
| List of Tables |
v |
| List of Figures |
vi |
| Abstract |
vii |
| |
I |
Objectives and Scope |
1 |
| |
A |
Background |
1 |
| B |
Objectives |
1 |
| C |
Technical Approach |
2 |
| II |
Summary of Progress |
8 |
| III |
Detailed Description of Technical Progress |
10 |
| IV |
Conclusions |
39 |
| V |
References |
40 |
| |
|
Appendix |
42 |
| |
A |
Transport limitation Calculations |
42 |
| |
| LIST OF TABLES |
|
| 1 |
Catalyst Preparation
Plans (Task 1) |
3 |
| 2 |
Experimental Plan |
5 |
| 3 |
Catalyst Compositions
and Codes |
11 |
| 4 |
H2 and CO
Chemisorption uptakes at 298 K - Iron and Cobalt Catalyst |
13 |
| 5 |
CO Turnover Numbers |
25 |
| 6 |
Selectivity data for Fe and Co Supported Catalysts |
34 |
| 7 |
Laboratories visited by principal investigator during contract period |
37 |
| 8 |
Visitors
and Speakers BYU catalysis laboratory, during contract period |
38 |
| |
|
LIST OF FIGURES |
|
| 1 |
Schedule of Proposed
Research Activities and Progress |
9 |
| 2 |
Fischer-Tropsch
reactor system |
14 |
| 3 |
High
Pressure Fischer-Tropsch Reactor |
15 |
| 4 |
Liquid and
Wax Trap |
17 |
| 5 |
Chromatograph Internals |
18 |
| 6 |
Temperature program and sampling scheme for chromatographic analysis |
19 |
| 7 |
Typical
Hydrocarbon Analysis |
20 |
| 8 |
Typical
fixed gases analysis |
21 |
| 9 |
Percent CO
conversion vs. reaction time for Co-S-102 |
23 |
| 10 |
Percent CO
Conversion, Percent CH4 and CO2 production vs.
reaction time for Co-B-A-101 |
24 |
| 11 |
CO
Turnover numbers for Iron and Cobalt catalysts |
26 |
| 12 |
Activation
energy plot for C0-B-A-101 |
27 |
| 13 |
Product
Distribution for Co-S-101 |
28 |
| 14 |
Product
Distribution for Co-S-102 |
29 |
| 15 |
Product
Distribution for Fe-S-100 |
30 |
| 16 |
Product
Distribution for Fe-S-102 |
31 |
| 17 |
Product
Distribution for Fe-ZSM-5 |
32 |
| 18 |
Product
Distribution for Fe-Silicalite |
33 |