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Higher mixed alcohols are produced from syngas contacting a catalyst in a reactor. The catalyst has a first component of molybdenum or tungsten, a second component of vanadium, a third component of iron, cobalt, nickel or palladium and optionally a fourth component of a promoter. The first component

Higher mixed alcohols are produced from syngas contacting a catalyst in a reactor. The catalyst has a first component of molybdenum or tungsten, a second component of vanadium, a third component of iron, cobalt, nickel or palladium and optionally a fourth component of a promoter. The first component forms alcohols, while the vanadium and the third component stimulates carbon chain growth to produce higher alcohols.

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1. A process for producing a mixture of alcohols from a syngas comprising the steps of: a) establishing a catalyst comprising crystalline molybdenum sulfide, crystalline cobalt sulfide and vanadium sulfide in a reactor;b) pressurizing said reactor to 100-10,000 psig;c) passing said syngas over said

1. A process for producing a mixture of alcohols from a syngas comprising the steps of: a) establishing a catalyst comprising crystalline molybdenum sulfide, crystalline cobalt sulfide and vanadium sulfide in a reactor;b) pressurizing said reactor to 100-10,000 psig;c) passing said syngas over said catalyst, the syngas comprising an amount of hydrogen to carbon monoxide of at least 0.5 hydrogen to 5.0 of carbon monoxide;d) heating said catalyst and said syngas to 200-375 degrees C.; ande)producing said mixed alcohols. 2. A process for producing an alcohol from a syngas as described in claim 1, wherein said step of establishing said catalyst in a reactor comprises the step of establishing crystalline molybdenum sulfide in a reactor such that a concentration of molybdenum in the catalyst is 33-43%, by weight, and the concentration of vanadium is 2-14%, by weight, among the molybdenum sulfide, the cobalt sulfide and the vanadium sulfide. 3. A process for producing an alcohol from a syngas as described in claim 1, wherein said step of establishing said catalyst in a reactor comprises the step of establishing crystalline molybdenum sulfide in a reactor such that a concentration in the catalyst of molybdenum is 36-43%, by weight, and the concentration of vanadium is 2-11%, by weight, among the molybdenum sulfide, the cobalt sulfide and the vanadium sulfide. 4. A process for producing an alcohol from a syngas as described, in claim 1, further comprising the step of establishing potassium in said reactor in the catalyst. 5. A process for producing an alcohol from a syngas as described in claim 1, wherein said step of establishing said catalyst in a reactor comprises the step of establishing crystalline molybdenum sulfide and crystalline vanadium sulfide in a single reaction zone in the reactor. 6. A process for producing an alcohol from a syngas as described in claim 1, wherein said step of producing said alcohol comprises the step of producing predominantly mixed alcohols, some ethers and hydrocarbons, in which the alcohol distribution, is comprised of 17 to 31 weight (wt) % methanol, 39-49 wt % ethanol, 19 to 29 wt % propanol, 4 to 12 wt % butanol, 0.1 to 5 wt % pentanol, the balance being 0 to 10 wt % hexanol, heptanol, octanol, nonanol, decanol, ethers, esters and hydrocarbons. 7. A process for producing an alcohol from a syngas as described in claim 1, wherein said crystalline cobalt sulfide comprises metallic cobalt. 8. A process for producing an alcohol from a syngas as described in claim 1, wherein said crystalline cobalt sulfide comprises zero valent cobalt. 9. A process for producing an alcohol from a syngas as described in claim 1, wherein said crystalline vanadium sulfide comprises metallic vanadium. 10. A process for producing an alcohol from a syngas as described in claim 1, wherein said crystalline vanadium sulfide comprises zero valent vanadium. 11. A process for producing an alcohol from a syngas as described in claim 1, further comprising the step of establishing a promoter in said reactor, wherein said promoter comprises potassium carbonate, zirconium and/or zirconium oxide. 12. A process for producing a mixture of alcohols from a syngas comprising the steps of: a) establishing a catalyst comprising crystalline molybdenum sulfide, crystalline cobalt sulfide and vanadium in a reactor, with the following amounts by weight: molybdenum33-43%vanadium 2-14%cobalt14-16% among the molybdenum sulfide, cobalt sulfide and vanadium;b) pressurizing said reactor to 100-10,000 psig;c) passing said syngas over said catalyst, the syngas comprising an amount of hydrogen to carbon monoxide of at least 0.5 hydrogen to 5.0 of carbon monoxide;d) heating said catalyst and said syngas to 200-375 degrees C.; ande) producing said mixed alcohols. 13. A process for producing an alcohol from a syngas as described in claim 12, wherein said step of establishing said catalyst in a reactor comprises the step of establishing crystalline molybdenum sulfide in a reactor such that a concentration in the catalyst of molybdenum is 36-43%, by weight, and the concentration of vanadium is 10-14%, by weight, among the molybdenum sulfide, the cobalt sulfide and the vanadium sulfide. 14. A process for producing a mixture of alcohols from a syngas comprising the steps of; a) establishing a catalyst comprising a first component with at least one element selected from the group consisting of molybdenum or tungsten in free or combined form, a second component comprising vanadium sulfide, and a third component with at least one element selected from the group consisting of iron, cobalt and nickel in free or combined form, the catalyst established in a reactor;b) pressurizing said reactor to 100-10000 psig;c) passing said syngas over said catalyst; the syngas comprising an amount of hydrogen to carbon monoxide of at least 0.5 hydrogen to 5.0 of carbon monoxide;d) heating said catalyst and said syngas to 200-375 degrees C.; ande) producing said mixed alcohols. 15. A process for producing an alcohol from a syngas as described in claim 3, wherein said step of establishing said catalyst in a reactor further comprises the step of establishing crystalline cobalt sulfide in the reactor such that a concentration of cobalt in the catalyst is 14-16% by weight, among the molybdenum sulfide, the cobalt sulfide and the vanadium sulfide. 16. A process for producing an alcohol from a syngas as described in claim 1, wherein the step of passing said syngas over said catalyst further comprises the step of the syngas comprising a range of hydrogen to carbon monoxide ratios of 0.5:5.0 to 1:1. 17. A process for producing an alcohol from a syngas as described in claim 12, wherein the step of passing said syngas over said catalyst thither comprises the step of the syngas comprising a range of hydrogen to carbon monoxide ratios of 0.5:5.0 to 1:1. 18. A process for producing an alcohol from a syngas as described in claim 14, wherein the step of passing said syngas over said catalyst further comprises the step of the syngas comprising a range of hydrogen to carbon monoxide ratios of 0.5:5.0 to 1:1.