Part 1 |
|
Abstract |
i |
Acknowledgements |
iv |
List of Symbols and Abbreviations |
v |
1. |
Introduction |
|
1.1 |
The Fischer-Tropsch Process; History, Past and Future Prospects |
1 |
1.2 |
The Spung Research Programme |
3 |
1.3 |
Scope of the Current Investigation |
4 |
2. |
Literature Review |
|
2.1 |
Cobalt; Chemical Properties and Catalytic Uses |
6 |
2.2 |
The nature and Role of Carbon in CO Hydrogenation over Supported Cobalt Catalyst |
9 |
2.3 |
Temperature Programmed Reduction (TPR) |
|
2.3.1 |
Introduction |
15 |
2.3.2 |
Reductive decomposition of Co(NO3)26H2O |
15 |
2.3.3 |
The extreme situations, CO3O4 and CoAl2O4 |
16 |
2.3.4 |
The effect of the cobalt loading |
18 |
2.3.5 |
The effect of the support |
21 |
2.3.6 |
The effect of different pretreatment conditions |
22 |
2.4 |
Fourier Transform Infrared (FTIR) Spectroscopy |
2.4.1 |
Introduction |
28 |
2.4.2 |
Carbon monoxide as a molecular probe |
28 |
2.4.3 |
Assignment of Vibrational bands for CO on supported cobalt catalysts |
30 |
2.4.4 |
Infrared ands for CO on CO3O4 |
36 |
2.4.5 |
Assignment of vibrational bands for CO on evaporated cobalt films |
37 |
2.4.6 |
The effect of metal loading on the infrared spectra of supported cobalt catalysts |
39 |
2.4.7 |
The Effect of hydrogen on adsorbed CO |
40 |
2.4.8 |
Infrared bands of adsorbed species in the frequency region 3050-2700 and 1800-1200 cm-1 |
42 |
2.5 |
CO Hydrogenation Activity and Selectivity |
2.5.1 |
Introduction |
44 |
2.5.2 |
Effect of metal loading and support on CO hydrogenation activity and selectivity |
44 |
3. |
Principles |
3.1 |
The Fischer-Tropsch Synthesis |
48 |
3.2 |
Temperature Programmed Reduction (TPR) |
56 |
3.3 |
Infrared Spectroscopy |
3.3.1 |
Theory |
57 |
3.3.2 |
Optical principles |
64 |
4. |
Experimental and Procedures |
|
4.1 |
Preparation of Catalysts |
69 |
4.2 |
Temperature Programmed Reduction (TPR) |
4.2.1 |
Apparatus |
70 |
4.2.2 |
Procedure |
70 |
4.3 |
Fourier Transform Infrared (FTIR) Spectroscopy |
4.3.1 |
Preparation of pressed disks for IR measurements |
72 |
4.3.2 |
High-Pressure infrared cells |
73 |
4.3.3 |
Gas Flow System |
75 |
4.3.4 |
Data acquisition |
75 |
4.3.5 |
FTIR-procedure |
75 |
4.4 |
Catalytic Activity Measurements |
4.4.1 |
Apparatus and analytical equipment |
78 |
4.4.2 |
Procedure |
80 |
4.5 |
Gravimetric Studies |
4.5.1 |
Gas Handling system and analytical equipment |
80 |
4.5.2 |
Procedure |
83 |
5. |
Results and Discussion |
|
Temperature Programmed Reduction Of Silica And Alumina Supported Cobalt Catalysts |
5.1 |
Temperature Programmed Reduction of Silica and Alumina Supported Cobalt Catalysts |
5.1.1 |
TPR-investigations of 0.82% Co/SiO2 and 4.7% Co/SiO2 |
85 |
5.1.2 |
TPR-investigations of 1% Co/y-Al2)3 and 4.6% Co/y-Al2O3 |
91 |
5.2 |
Fourier Transform Infrared (FTIR) Investigations |
5.2.1 |
Introduction |
97 |
5.2.2 |
A brief study of SiO2 |
98 |
5.2.3 |
Hydrogenation of CO over silica supported cobalt catalysts with different metal loading |
|
5.2.3.1 |
CO spectral region for 0.82% Co/SiO2 |
100 |
5.2.3.2 |
CO spectral region for 4.7% Co/SiO2 H2/CO=2, Ptot=6 bar, T-473-573K |
102 |
5.2.3.3 |
CO spectral region for 4.7% Co/SiO2 H2/CO=3, Ptot=6 bar, T=473-573K |
104 |
5.2.3.4 |
CO spectral region for 4.7% Co/SiO2 H2/CO=3, Ptot=6r bar, T=473-573K |
111 |
5.2.3.5 |
Estimation of the heat of adsorption of CO on 4.7% Co/SiO2 |
129 |
5.2.3.6 |
Estimations of the amount of adsorbed CO on 4.7% Co/SiO2 At reaction conditions |
132 |
5.2.4
Part 2 |
Hydrogenation of CO over alumina supported Co Catalysts with Different metal loading |
|
5.2.4.1 |
CO spectral region for 1% Co/y-Al2O3 |
135 |
5.2.4.2 |
CO spectral region for 4.6% Co/y-Al2O3 H2/CO=2, |
144 |
5.2.5 |
Bands observed in the 3050-2800 cm-1 spectral range over silica alone and silica supported Co Catalysts (0.82 and 4.7% Co/SiO2) at different reaction conditions |
159 |
5.2.6 |
Bands observed in the 3050-2800 cm-1 spectral region over 4.6% Co/y-Al2O3 and pure alumina during CO hydrogenation |
171 |
5.2.7 |
Discussion of the behavior and nature of the absorption bands observed in the frequency range 3050-2800 cm-1 |
173 |
5.2.8 |
Bands observed in the 1800-1200 cm-1 spectral range during CO hydrogenation over silica and alumina supported Co Catalysts |
|
5.2.8.1 |
Introduction |
181 |
5.2.8.2 |
4.7% Co/SiO2 |
181 |
5.2.8.3 |
4.6% Co/y-Al2O3 NS Y-Al2O3 |
196 |
5.3 |
Catalytic Activity and Selectivity |
|
5.3.1 |
Introduction |
222 |
5.3.2 |
CO hydrogenation activity and selectivity of silica and alumina Supported cobalt catalysts |
222 |
5.4 |
Gravimetric Investigations of 4.7% Co/SiO2 and 4.6% Co/y-Al2O3 During CO Hydrogenation |
|
5.4.1 |
Introduction |
231 |
5.4.2 |
Gravimetric studies of 4.7% Co/SiO2 |
232 |
5.4.3 |
Gravimetric studies of 4.6% Co/y-Al2O3 |
235 |
5.4.4 |
Discussion of the weight curves obtained during CO hydrogenation over silica, alumina, 4.6% Co/y-Al2O3 and 4.7% Co/SiO2 |
242 |
6. |
Summary and Conclusions |
6.1 |
Temperature Programmed Reduction |
269 |
6.2 |
Infrared Spectroscopy |
269 |
6.3 |
CO Hydrogenation Activity and Selectivity |
271 |
6.4 |
Gravimetry |
272 |
7. |
References |
274 |
Appendices |
284 |