|
Return to DOE Report Table of Contents
Return to Catalysts for the Indirect
Liquefaction of Coal - 1979 to 1986
New Catalysts for the Indirect Liquefaction of Coal.
Third Quarterly Technical Report for February 1 to April 30, 1982
Gordon A. Melson
Virginia Commonwealth University
In this pdf format, this
document has 14 pages and is 364kb.
Table of Contents
|
Abstract |
2 |
| 1 |
All catalysts are effective for synthesis gas
conversion |
3 |
| 2 |
Increase in particle size of the iron component is reflected in an
increase in % CO and % H2 conversion (Table 1 and Figure
1). |
3 |
| 3 |
All catalysts are effective for the water gas shift reaction |
4 |
| 4 |
The % hydrocarbons obtained in the reactor effluent increases at the
higher temperature (Figure 2) |
4 |
| 5 |
Significant quantities of low molecular weight (C1-C4)
hydrocarbons are obtained (Figures 3 and 4). |
4 |
| 6 |
All catalysts produce significant quantities of liquid hydrocarbons,
C5 + (oil) (Figure 4) |
4 |
| 7 |
The Fe/mordenite catalysts with the stronger acidity (SiO2/Al2O3
ratio = 17.4) produces no wax. |
4 |
| 8 |
The Fe/mordenite catalyst with the strongest acidity (SiO2/Al2O3
ratio = 17.4) produces the highest % aromatics in the liquid
hydrocarbon product (Figure 5). |
4 |
| 9 |
The Fe/mordenite catalyst with SiO2/Al2O3
ratio = 11.4 produces |
4 |
|
Papers Presented |
7 |
| 