초록 ▼

An improved skeletal iron catalyst is provided for use in Fischer-Tropsch synthesis reactions for converting CO and H2 to hydrocarbon products. The skeletal iron catalyst is manufactured using iron and a removable non-ferrous component such as aluminum. The iron and removable non-ferrous component a

An improved skeletal iron catalyst is provided for use in Fischer-Tropsch synthesis reactions for converting CO and H2 to hydrocarbon products. The skeletal iron catalyst is manufactured using iron and a removable non-ferrous component such as aluminum. The iron and removable non-ferrous component are mixed together to form a precursor catalyst and then a portion of the removable non-ferrous component is removed to leave a skeletal iron catalyst. One or more first promoter metals and optionally one or more second promoter metals are incorporated into the skeletal iron catalyst either by blending the promoter into the precursor catalyst during the formation thereof or by depositing the promoter on the skeletal iron. The first promoter metals comprises a metal selected from the group consisting of titanium, zirconium, vanadium, cobalt, molybdenum, tungsten, and platinum-group metals. The first promoter metal is selected to improve the yield of C5+ hydrocarbons when the skeletal iron catalyst is used in a Fischer-Tropsch reaction.

대표청구항 ▼

What is claimed is: 1. A Fischer-Tropsch catalyst having a skeletal iron structure and increased catalytic selectivity for C5+ manufactured according to a method, comprising: forming a solid catalyst precursor composition by: melting together iron metal and a removable non-ferrous component compris

What is claimed is: 1. A Fischer-Tropsch catalyst having a skeletal iron structure and increased catalytic selectivity for C5+ manufactured according to a method, comprising: forming a solid catalyst precursor composition by: melting together iron metal and a removable non-ferrous component comprising one or more of aluminum, antimony, silicon, tin, or zinc to form a molten iron alloy; and cooling the molten iron alloy to yield the solid catalyst precursor composition; removing at least a portion of the removable non-ferrous component from the solid catalyst precursor composition to form a skeletal iron structure composed of a porous metal framework having a specific surface area of at least about 20 m2/g, wherein the porous metal framework is comprised of fused iron metal and void spaces where the removable non-ferrous component was removed; depositing one or more first promoter metals on the skeletal iron structure or incorporating the one or more first promoter metals into the solid catalyst precursor composition during formation thereof or both, wherein the one or more first promoter metals comprise at least one metal selected from the group consisting of titanium, zirconium, vanadium, cobalt, molybdenum, tungsten, and platinum-group metals, wherein the one or more first promoter metals increase catalytic selectivity for C5+ in a Fischer-Tropsch synthesis compared to a skeletal iron catalyst in the absence of the one or more first promoter metals; and optionally, depositing one or more second promoter metals on the skeletal iron structure or incorporating one or more second promoter metals into the catalyst precursor composition during the formation thereof or both, wherein the one or more second promoter metals comprise at least one metal selected from the group consisting of manganese, calcium, copper, chromium, potassium, and magnesium. 2. A Fischer-Tropsch catalyst as claimed in claim 1, wherein the first promoter metal comprises at least one of titanium, zirconium, vanadium, cobalt, or molybdenum. 3. A Fischer-Tropsch catalyst as claimed in claim 1, wherein the first promoter metal comprises titania. 4. A Fischer-Tropsch catalyst as claimed in claim 1, wherein the first promoter metal is incorporated into the solid catalyst precursor composition during the formation thereof. 5. A Fischer-Tropsch catalyst as claimed in claim 1, wherein the first promoter metal is deposited on the skeletal iron structure after formation thereof. 6. A Fischer-Tropsch catalyst as claimed in claim 1, wherein the solid catalyst precursor composition and the skeletal iron structure formed therefrom comprise a plurality of particles having a particle size between about 10 microns and about 10 mm. 7. A Fischer-Tropsch catalyst as claimed in claim 6, wherein the plurality of particles are formed by (i) combining at least the iron metal, the removable non-ferrous component, and the first promoter metal to form a solid composition, (ii) pulverizing the solid composition to form the plurality of particles, and (iii) removing the removable non-ferrous component. 8. A Fischer-Tropsch catalyst as claimed in claim 6, wherein the particles have a particle size between about 10 microns and about 2 mm. 9. A Fischer-Tropsch catalyst as claimed in claim 6, wherein the particles have a particle size between about 1 mm and about 10 mm. 10. A Fischer-Tropsch catalyst as claimed in claim 1, wherein the removable non-ferrous component is removed by leaching with a caustic solution. 11. A catalytic Fischer-Tropsch synthesis process, comprising feeding H2 and CO into a reactor containing the Fischer-Tropsch catalyst manufactured according to claim 1 and withdrawing from the reactor a hydrocarbon product. 12. A Fischer-Tropsch catalyst having a skeletal iron structure and increased catalytic selectivity for C5+ manufactured according to a method, comprising: forming a solid catalyst precursor composition by: melting together: iron metal; manganese or an oxide thereof; a removable non-ferrous component comprising one or more of aluminum, antimony, silicon, tin, or zinc; and one or more first promoter metals, wherein the one or more first promoter metals comprise a metal selected from the group consisting of titanium, zirconium, vanadium, cobalt, and molybdenum to form a molten iron alloy; and cooling the molten iron alloy to yield the solid catalyst precursor composition; pulverizing the solid catalyst precursor to form a plurality of smaller precursor particles; and removing at least a portion of the removable non-ferrous component from the precursor particles to form the Fischer-Tropsch catalyst having a skeletal iron structure composed of a porous metal framework having a specific surface area of at least about 20 m2/g, wherein the porous metal framework is comprised of fused iron metal and void spaces where the removable non-ferrous component was removed; wherein the one or more first promoter metals increase catalytic selectivity for C5+ in a Fischer-Tropsch synthesis compared to a skeletal iron catalyst in the absence of the one or more first promoter metals. 13. A Fischer-Tropsch catalyst as claimed in claim 12, wherein the one or more first promoter metals comprise titanium. 14. A Fischer-Tropsch catalyst as claimed in claim 12, further comprising impregnating the Fischer-Tropsch catalyst with potassium. 15. A catalytic Fischer-Tropsch synthesis process, comprising feeding H2 and CO into a reactor containing the Fischer-Tropsch catalyst manufactured according to claim 12 and withdrawing from the reactor a hydrocarbon product. 16. A Fischer-Tropsch catalyst having a skeletal iron structure and increased catalytic selectivity for C5+, comprising: a skeletal iron catalyst comprising from about 70 wt % to about 90 wt % iron in the form of a skeletal iron structure composed of a porous metal framework having a specific surface area of at least about 20 m2/g, wherein the porous metal framework is comprised of fused iron metal and void spaces formed by removing a removable non-ferrous component from the fused metal iron, the skeletal iron catalyst further comprising: from about 0.01 wt % to about 10 wt % of one or more first promoter metals comprising at least one metal selected from the group consisting of titanium, zirconium, vanadium, cobalt, molybdenum, tungsten, and platinum-group metals; and from about 0.01 wt % to about 20 wt % of one or more second promoter metals comprising a metal selected from the group consisting of manganese, calcium, copper, chromium, potassium, and magnesium, wherein the one or more first promoter metals increase catalytic selectivity for C5+ in a Fischer-Tropsch synthesis compared to a skeletal iron catalyst in the absence of the one or more first promoter metals. 17. A Fischer-Tropsch catalyst as claimed in claim 16, wherein the one or more first promoter metals comprise titanium. 18. A Fischer-Tropsch catalyst as claimed in claim 16, wherein the one or more first promoter metals have a weight percent of at least about 1%. 19. A Fischer-Tropsch catalyst as claimed in claim 16, wherein the one or more promoter metals are deposited on a surface of the skeletal iron structure. 20. A Fischer-Tropsch catalyst as claimed in claim 16, wherein the one or more first promoter metals are substantially evenly dispersed throughout the skeletal iron structure. 21. A Fischer-Tropsch catalyst as claimed in claim 16, wherein the Fischer-Tropsch catalyst comprises a plurality of particles. 22. A Fischer-Tropsch catalyst as claimed in claim 21, wherein the particles have a particle size in a range of about 10 microns to about 2 mm. 23. A Fischer-Tropsch catalyst as claimed in claim 21, wherein the particles have a particle size in a range of about 1 mm to about 10 mm. 24. A catalytic Fischer-Tropsch synthesis process, comprising feeding H2 and CO into a reactor containing the Fischer-Tropsch catalyst of claim 16 and withdrawing from the reactor a hydrocarbon product.