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Table of Contents
Catalyst and Process Development for Synthesis Gas Conversion
to Isobutylene.
Final Report. Contract Duration September 1, 1990 to January 31,
1994
Co-Principal Investigators
Anthony, Rayford, G.
Akgerman, Aydin
Project Team
Philip, Dr. C. V.
Erkey, Dr. CAn
Zhenatao, Jeffrey Feng
Postula, Walter S.
Wang, Jianhua
Texas A&M University
Table of Contents
|
Extended Abstract |
iii |
Table of Contents |
vi |
List of Tables |
viii |
List of Figures |
xi |
Chapter |
Section 1
1278kb |
I |
Introduction |
1 |
|
Isobutylene Synthesis |
2 |
Reaction Mechanism |
3 |
Zirconia Synthesis by Precipitation |
5 |
Kinetics and Therymodynamics |
6 |
Modeling |
10 |
II |
Experimental |
11 |
|
Catalyst Preparation |
11 |
Catalyst Characterization |
13 |
Materials |
13 |
Apparatus and Procedure |
14 |
Section 2
2835kb |
III |
Results and Discussion |
18 |
|
Catalyst Characterization |
18 |
Catalyst Activity and Selectivity |
23 |
Equation Development for the Modeling of
Carbon Monoxide Conversion (Fixed Bed) |
43 |
Results of Modelingof Product Distribution
(Fixed Bed) |
48 |
Modeling of Slurry Reactors |
49 |
Section 3
1037kb |
IV |
Conclusions |
53 |
|
Nomenclature |
55 |
References |
56 |
Appendix A Relationship Between wt% and Carbon Conversion |
60 |
Appendix B Rate Equation Parameters, Surface Intermediates and
Simplified Mechanisms |
62 |
Section 4
989kb |
Appendix C Publications, Converence Papers, and Presentations based
on this work |
77 |
Appendix D Tables |
80 |
Section 5
1297kb |
Appendix E Figures |
109 |
|