초록 ▼

A unique process and catalyst is described that operates efficiently for the direct production of a high cetane diesel type fuel or diesel type blending stock from stoichiometric mixtures of hydrogen and carbon monoxide. This invention allows for, but is not limited to, the economical and efficient

A unique process and catalyst is described that operates efficiently for the direct production of a high cetane diesel type fuel or diesel type blending stock from stoichiometric mixtures of hydrogen and carbon monoxide. This invention allows for, but is not limited to, the economical and efficient production high quality diesel type fuels from small or distributed fuel production plants that have an annual production capacity of less than 10,000 barrels of product per day, by eliminating traditional wax upgrading processes. This catalytic process is ideal for distributed diesel fuel production plants such as gas to liquids production and other applications that require optimized economics based on supporting distributed feedstock resources.

대표청구항 ▼

1. A process for the production of a hydrocarbon mixture comprising the steps of: a) reducing a supported catalyst to provide a reduced catalyst;b) using the reduced catalyst in a fixed bed reactor;c) reacting a feed gas that contains hydrogen and carbon monoxide with the reduced catalyst to produce

1. A process for the production of a hydrocarbon mixture comprising the steps of: a) reducing a supported catalyst to provide a reduced catalyst;b) using the reduced catalyst in a fixed bed reactor;c) reacting a feed gas that contains hydrogen and carbon monoxide with the reduced catalyst to produce a hydrocarbon product stream, wherein the hydrocarbon product stream comprises light gases, diesel fuel and a wax;d) condensing the diesel fuel and wax, wherein the diesel fuel comprises more than ⅔ of the diesel fuel and wax together, and wherein a majority of hydrocarbons in the diesel fuel are C8-C24 hydrocarbons. 2. The process of claim 1, wherein the catalyst has: a pore diameter greater than 80 angstroms and;a crush strength of greater than 3 lbs/mm and;a BET surface area of greater than 110 m2/g;a dispersion value between 2% and 10%. 3. The process of claim 1, wherein the supported catalyst comprises a lobed support with more than four lobes and an effective pellet radius of less than 600 microns. 4. The process of claim 1, wherein the supported catalyst further comprises about 0.01 weight percent to about 2.0 weight percent of a promoter selected from the group consisting of cerium, ruthenium, lanthanum, platinum, rhenium, gold, nickel, or rhodium and a combination thereof. 5. The process of claim 1, wherein the catalyst is supported on alumina. 6. The process of claim 1, wherein the diesel fuel and wax are condensed into a single vessel. 7. A process for the production of a hydrocarbon mixture comprising the steps of: a) reducing an alumina supported catalyst, wherein the catalyst includes cobalt as a catalytically active metal, to provide a reduced catalyst;b) using the reduced catalyst in a fixed bed reactor;c) reacting a feed gas that contains hydrogen and carbon monoxide with the reduced catalyst to produce a hydrocarbon product stream, wherein the hydrocarbon product stream comprises light gases, diesel fuel and a wax, wherein a majority of hydrocarbons in the diesel fuel are C8-C24 hydrocarbons, and wherein the diesel fuel is produced without the hydroprocessing of wax. 8. The process of claim 7, wherein the catalyst has a pore diameter greater than 80 angstroms, a crush strength greater than 3 lbs/mm, a BET surface area of greater than 110 m2/g, and a dispersion value between 2% and 10%. 9. The process of claim 7, wherein the supported catalyst comprises a lobed support, and wherein the supported catalyst comprises about 0.01 weight percent to about 2.0 weight percent of a promoter selected from a group consisting of cerium, ruthenium, lanthanum, platinum, rhenium, gold, nickel or rhodium and a combination thereof. 10. The process of claim 7, wherein the diesel fuel and wax are condensed into a single vessel. 11. The process according to claim 7, wherein the supported catalyst comprises a lobed support, and wherein the supported catalyst comprises about 0.01 weight percent to about 2.0 weight percent of a promoter selected from a group consisting of cerium, ruthenium, lanthanum, platinum, rhenium, gold, nickel or rhodium and a combination thereof. 12. A process for the production of a hydrocarbon mixture comprising the steps of: a) reducing an alumina supported catalyst, wherein the catalyst includes cobalt as a catalytically active metal, in-situ in a fixed bed reactor to provide a reduced catalyst;b) using the reduced catalyst in a fixed bed reactor;c) reacting a feed gas that contains hydrogen and carbon monoxide with the reduced catalyst to produce a hydrocarbon product stream, wherein the hydrocarbon product stream comprises light gases, diesel fuel and a wax;d) introducing the product stream into a single vessel and condensing the product stream into two liquid fractions in the single vessel, wherein the two liquid fractions are a top fraction and a bottom fraction, and wherein the top fraction contains the diesel fuel and the bottom fraction contains water. 13. The process according to claim 12, wherein the catalyst has a pore diameter greater than 80 angstroms, a crush strength of greater than 3 lbs/mm, a BET surface area of greater than 110 m2/g and a dispersion value between 2% and 10%. 14. The process according to claim 12, wherein the supported catalyst comprises a lobed support, and wherein the supported catalyst comprises about 0.01 weight percent to about 2.0 weight percent of a promoter selected from a group consisting of cerium, ruthenium, lanthanum, platinum, rhenium, gold, nickel or rhodium and a combination thereof. 15. The process according to claim 13, wherein the supported catalyst comprises a lobed support, and wherein the supported catalyst comprises about 0.01 weight percent to about 2.0 weight percent of a promoter selected from a group consisting of cerium, ruthenium, lanthanum, platinum, rhenium, gold, nickel or rhodium and a combination thereof.