| Patent Number |
Title Of Patent |
Date Issued |
| 7351679 |
Fischer-tropsch catalyst, preparation, and use thereof |
April 1, 2008 |
| Embodiments include a catalyst for use in a Fischer-Tropsch synthesis reaction which comprises cobalt supported on alumina. In some embodiments, the alumina support may have specific surface area of less than 50 m.sup.2/g and/or may be least 10% .alpha.-alumina. |
| 5116879 |
Process using a supported catalyst for hydrocarbon synthesis |
May 26, 1992 |
| A process for converting synthesis gas, a mixture of hydrogen and carbon monoxide, into a mixture of predominately paraffinic hydrocarbons using a catalyst which includes catalytically active amounts of cobalt and a loading-insensitive second metal selected from the group consisting of |
| 5102851 |
Supported catalyst for hydrocarbon synthesis |
April 7, 1992 |
| A catalyst for converting synthesis gas, a mixture of hydrogen and carbon monoxide, into a mixture of predominately paraffinic hydrocarbons. The catalyst includes catalytically active amounts of cobalt and a loading-insensitive second metal selected from the group consisting of plati |
| 4880763 |
Catalyst for production of hydrocarbons |
November 14, 1989 |
| A catalyst for converting synthesis gas composed of hydrogen and carbon monoxide to hydrocarbons. The catalyst includes cobalt in catalytically active amounts up to about 60 wt % of the catalyst, rhenium in amounts of about 0.5 to 50 wt % of the cobalt content of the catalyst and an alka |
| 4857559 |
Process for production of hydrocarbons |
August 15, 1989 |
| A process for converting synthesis gas composed of hydrogen and carbon monoxide to hydrocarbons. The process includes the step of contacting at reaction conditions a synthesis gas feed to a catalyst which includes cobalt in catalytically active amounts up to about 60 wt % of the catalyst |
| 4801573 |
Catalyst for production of hydrocarbons |
January 31, 1989 |
| A catalyst for converting synthesis gas composed of hydrogen and carbon monoxide to hydrocarbons. The catalyst includes cobalt in catalytically active amounts up to about 60 wt % of the catalyst and rhenium in catalytically active amounts of about 0.5 to 50 wt % of the cobalt content |
