Section 1
1249kb |
List of Figures |
xii |
List of Tables |
xxviii |
1 |
The Fischer Tropsch Synthesis |
1 |
|
1.1 |
Historical Overview |
1 |
1.2 |
Primary FT Reactions and
Secondary Complicating Reactions |
2 |
Section 2
1086kb |
2 |
The Product Distribution and
Reaction Mechanism |
3 |
|
2.1 |
The Product Distribution |
3 |
|
2.1.1 |
Hydrocarbon Products |
3 |
2.1.2 |
Oxygenated Products |
5 |
2.2 |
Reaction Mechanisms |
6 |
|
2.2.1 |
The Carbidic Intermediate |
8 |
2.2.2 |
The Oxygen Containing Intermediate |
13 |
2.2.3 |
Carbidic Initiation/CO Insertion |
16 |
Section 3
1497kb |
2.3 |
Surface Studies on FT Catalysts |
17 |
|
2.3.1 |
IR Spectroscopy |
17 |
2.3.2 |
Electron Spectroscopies |
19 |
2.4 |
Hydrogenation/Isomerization
Reaction Mechanisms |
20 |
3 |
Experimental Methods and Catalyst
Characterization |
24 |
|
3.1 |
Catalyst Preparation |
24 |
3.2 |
Characterization Methods and
Results |
25 |
|
3.2.1 |
Mossbauer Spectroscopy; Theory
and Results |
25 |
|
3.2.1.1 |
Theory |
25 |
3.2.1.2 |
Experimental |
33 |
Section 4
1257kb |
3.2.2 |
Catalyst Characterization |
34 |
|
3.2.2.1 |
Fe Catalyst |
34 |
3.2.2.2 |
FeCo Catalyst |
38 |
3.2.2.3 |
Co Catalyst |
41 |
3.2.3 |
Catalytic Surface Area
Measurements |
41 |
3.3 |
Reactor and Analytical Equipment |
43 |
|
3.3.1 |
The Differential Flow Reactor |
43 |
3.3.2 |
Feed Mixtures |
46 |
Section 5
939kb |
3.3.3 |
Gas Chromatograph Calibration
Procedure |
47 |
3.3.4 |
Gas Chromatographs Employed |
48 |
3.3.5 |
Rate Data Analysis |
53 |
Section 6
517kb |
4 |
Reaction Studies Using CO/H2
Mixtures |
56 |
|
4.1 |
CO Activity Studies |
56 |
|
4.1.1 |
Fe Catalyst |
57 |
4.1.2 |
Co Catalyst |
60 |
4.1.3 |
FeCo Catalyst |
61 |
Section 7
524kb |
4.1.4 |
Comparison of Rate Data with
Proposed Kinetic Expressions |
65 |
4.1.5 |
Methane Differential
Selectivity |
66 |
4.1.6 |
Relative Methanol Activities |
72 |
Section 8
630kb |
4.1.7 |
Activity Maintenance Studies |
74 |
4.2 |
Water Gas Shift Activity |
78 |
|
4.2.1 |
Effects of Pressure and Feed
Composition |
78 |
4.2.2 |
Shift Equilibrium and Rate
Models |
80 |
Section 9
512kb |
4.2.3 |
Effects of Water Vapor |
86 |
4.3 |
Low Molecular Weight Product
Yields |
88 |
|
4.3.1 |
Olefin Yields for the Fe
Catalyst with the 1/3 CO/H2 Feed |
89 |
4.3.2 |
Olefin Yields for the Fe Catalyst with the 1/3 CO/H2 Feed |
93 |
Section 10
627kb |
4.3.3 |
Olefin Yields for the Co
Catalyst with the 1/3 CO/H2 Feed |
96 |
4.3.4 |
Comparison of the C2 and
C3 Yields and Olefin Selectivities for all three Catalysts |
96 |
4.3.5 |
Methane Yields using the 1/3 CO/H2 Feed |
101 |
Section 11
779kb |
4.3.6 |
Olefin Yields and
Selectivities using the 1/1 CO/H2 Feed |
108 |
Section 12
775kb |
4.3.7 |
Methane Yields using the 1/1
CO H2 Feed |
124 |
4.4 |
Steady State Product
Distributions |
129 |
|
4.4.1 |
Overall Product Distributions |
129 |
Section 13
736kb |
4.4.2 |
Shifts in the Product
Distribution due to conversion and pressure |
140 |
4.5 |
Schulz Flory Parameterization |
153 |
Section 14
866kb |
|
4.5.1 |
Fe Catalyst |
155 |
4.5.2 |
Co Catalyst |
159 |
4.5.3 |
FeCo Catalyst |
159 |
4.5.4 |
Growth Probability dependence
on pressure and feed rates |
162 |
4.5.5 |
C1 Product Yields |
167 |
Section 15
887kb |
4.6 |
Transient Studies on a Fully
Carburized Iron Catalyst |
172 |
|
4.6.4 |
1/3 CO/H2 Feed |
184 |
Section 16
682kb |
4.6.5 |
Production of CO2 and
CH3OH
through a Common Intermediate |
188 |
|
4.6.5.1 |
Transient Response of
Oxygenated Products |
188 |
4.6.5.2 |
Proposed Shift Reaction
Mechanisms |
191 |
4.6.5.3 |
Proposed Mechanisms for CH3OH Production |
192 |
5 |
Synthesis Studies in Olefin Enhanced
Feeds |
194 |
|
5.1 |
Methane Activities |
195 |
|
5.1.1 |
Fe Catalyst |
195 |
5.1.2 |
FeCo Catalyst |
197 |
5.1.3 |
Co Catalyst |
197 |
5.1.4 |
Discussion on 1-Pentene
Hydrocracking |
200 |
Section 17
1095kb |
5.2 |
Product Yields and Selectivities
for Olefin Containing Feeds |
201 |
|
5.2.1 |
Hydrocarbon Yields with the
Ethylene containing Feed |
201 |
5.2.2 |
Hydrocarbon Yields with the
1-Pentene containing Feed |
212 |
|
5.2.2.1 |
Fe Catalyst |
213 |
5.2.2.2 |
FeCo Catalyst |
213 |
Section 18
1139kb |
5.2.2.3 |
Co Catalyst |
219 |
5.2.2.4 |
Hydrocracking over the Co
Catalyst |
222 |
5.2.3 |
Methanol and Carbon Dioxide
Yields |
224 |
5.3 |
Schultz Flory Parameterization |
227 |
|
5.3.1 |
Fe Catalyst |
228 |
5.3.2 |
Co Catalyst |
230 |
Section 19
953kb |
5.3.3 |
FeCo Catalyst |
238 |
5.3.4 |
Mechanistic Implications |
238 |
5.4 |
Selectivity Studies and
Secondary Reactions |
248 |
|
5.4.1 |
Olefin/Paraffin Selectivities
Using the Ethylene Enhanced Feed |
248 |
|
5.4.1.1 |
Fe Catalyst |
248 |
5.4.1.2 |
Co Catalyst |
250 |
Section 20
767kb |
5.4.1.3 |
FeCo Catalyst |
254 |
5.4.2 |
Hydrogenation of Feed Gas
Ethylene |
258 |
Section 21
1006kb |
5.4.3 |
Proposed Reaction Network for
the Primary and Secondary FT Reactions |
266 |
5.4.4 |
Olefin/Paraffin Selectivities
in the 1-Pentene Enhanced Feed |
276 |
Section 22
763kb |
5.4.5 |
Secondary Reactions Involving
1-Pentene |
284 |
5.4.6 |
Proposed Reaction Network for
the C5 Products |
291 |
Section 23
997kb |
6 |
Review of Results and Conclusions |
298 |
|
6.1 |
Summary of Observed General
Behavior of the FT Synthesis |
298 |
|
6.1.1 |
Result Summary of Chapter 4 |
298 |
6.1.2 |
Result Summary of Chapter 5 |
300 |
6.2 |
Summary of the Observed Kinetic
Differences Between the Alloy and Pure Component Catalysts |
302 |
|
6.2.1 |
Result Summary of Chapter 4 |
302 |
6.2.2 |
Result Summary of Chapter 5 |
303 |
6.3 |
Generalized Reaction Sequence
Involving Multiple Surface Intermediates |
304 |
7 |
Some Considerations for Future FT
Research |
306 |
Section 24
565kb |
Appendix I: GC Calibration Mixtures |
315 |
Appendix II: Reaction Rate Analysis |
318 |
Appendix III: Boudouard Reaction Equilibrium Constant |
324 |
Appendix IV: Adsorption Calculations Under FT
Conditions |
325 |
Section 25
546kb |
Appendix V: Various Product Yields Using the
Olefin Containing Feeds |
327 |
Appendix VI: Methane Activities for the Co
catalyst with various CO/H2 Feeds |
336 |
List of References |
337 |
Vita |
334 |