초록 ▼

A particulate catalyst comprises an intimate mixture of cobalt and aluminum compounds at an atomic ratio in the range 10:1 to 2:1 (Co:Al), which when reduced at 425° C., has a cobalt surface area as measured by hydrogen chemisorption at 150° C. of at least 30 m2/g of catalyst. The catalyst

A particulate catalyst comprises an intimate mixture of cobalt and aluminum compounds at an atomic ratio in the range 10:1 to 2:1 (Co:Al), which when reduced at 425° C., has a cobalt surface area as measured by hydrogen chemisorption at 150° C. of at least 30 m2/g of catalyst. The catalyst is prepared by sequential precipitation of cobalt with aluminum ions in the presence of an alkaline precipitation agent. The catalyst may be used for the hydrogenation of unsaturated compounds or the Fischer-Tropsch synthesis of hydrocarbons.

대표청구항 ▼

The invention claimed is: 1. A process for the Fischer-Tropsch synthesis of hydrocarbons comprising the step of reacting a mixture of carbon monoxide and hydrogen in the presence of a particulate catalyst comprising a precipitated intimate mixture of precipitated cobalt and aluminum compounds in wh

The invention claimed is: 1. A process for the Fischer-Tropsch synthesis of hydrocarbons comprising the step of reacting a mixture of carbon monoxide and hydrogen in the presence of a particulate catalyst comprising a precipitated intimate mixture of precipitated cobalt and aluminum compounds in which the cobalt compounds are supported on cobalt-aluminum compounds, said mixture having a cobalt content ≧60% wt and a cobalt and aluminum at an atomic ratio in the range 10:1 to 2:1 (Co:Al), which when reduced at 425° C., has a cobalt surface area as measured by hydrogen chemisorption at 150° C. of at least 30 m2/g of catalyst wherein the catalyst is prepared by steps comprising: (i) precipitating an insoluble cobalt compound from an aqueous solution of a cobalt salt with an excess alkaline precipitating agent, (ii) adding a soluble aluminum compound, (iii) aging the resulting precipitate in suspended form, (iv) recovering and drying the catalyst composition, and (v) activating the catalyst by reduction using a hydrogen-containing gas. 2. A process according to claim 1 further comprising a step of calcining of the dried catalyst composition. 3. A process according to claim 1 wherein the cobalt salt is selected from the group consisting of a nitrate, sulfate, acetate, chloride and formate. 4. A process according to claim 1 wherein the cobalt salt is cobalt nitrate. 5. A process according to claim 1 wherein the precipitating agent is selected from the group consisting of an alkali metal hydroxide, alkali metal carbonate, alkali metal bicarbonate, ammonium hydroxide, ammonium carbonate, and a mixture thereof. 6. A process according to claim 1 wherein the precipitating agent is selected from the group consisting of sodium hydroxide, sodium carbonate and mixtures thereof. 7. A process according to claim 1 wherein the precipitation is effected at a pH in the range 7-10 at a temperature below 50° C. 8. A process according to claim 1 wherein the soluble aluminum compound is selected from the group consisting of aluminum nitrate, sodium aluminate and alumina that dissolves at least partly in the excess alkali. 9. A process according to claim 8 wherein the soluble aluminum compound is sodium aluminate. 10. A process according to claim 1 wherein aging is performed until >50% of the aluminum is in the form of cobalt aluminum compounds. 11. A process according to claim 1 wherein the aging is performed at a pH in the range of 6-11 at a temperature in the range 10-100° C. 12. A process according to claim 1 wherein the mixture of carbon monoxide and hydrogen used for the Fischer-Tropsch synthesis of hydrocarbons is a synthesis gas having a hydrogen:carbon monoxide ratio in the range 1.7-2.5:1. 13. A process according to claim 1 wherein the Fischer-Tropsch synthesis of hydrocarbons is performed in a continuous or batch process using one or more stirred slurry-phase reactors, bubble-column reactors, loop reactors or fluidized bed reactors. 14. A process according to claim 1 wherein the Fischer-Tropsch synthesis of hydrocarbons is operated at pressures in the range 0.1-10 MPa and temperatures in the range 150-350° C. 15. A process according to claim 1 wherein the Co:Al atomic ratio is in the range 5:1 to 2.5:1. 16. A process according to claim 1 wherein the BET surface area of the catalyst prior to reduction is between 50 and 250 m2/g. 17. A process according to claim 1 wherein the catalyst further comprises one or more additives or promoters. 18. A process according to claim 1 wherein the catalyst further comprises at least one additive selected from the group consisting of compounds of molybdenum, nickel, copper, iron, manganese, titanium, zirconium, lanthanum, cerium, chromium, magnesium, and zinc. 19. A process according to claim 1 wherein the catalyst further comprises at least one promoter selected from the group consisting of rhodium, iridium, ruthenium, rhenium, platinum, and palladium.