Cobalt-molybdenum sulfide catalyst materials and methods for ethanol production from syngas
The present invention provides methods and compositions for the chemical conversion of syngas to alcohols. The invention includes catalyst compositions, methods of making the catalyst compositions, and methods of using the catalyst compositions. Certain embodiments teach compositions for catalyzing the conversion of syngas into products comprising at least one C 1 -C 4 alcohol, such as ethanol. These compositions generally include cobalt, molybdenum, and sulfur. Preferred catalyst compositions for converting syngas into alcohols include cobalt associated with sulfide in certain preferred stoichiometries as described and taught herein.
1. A method of producing at least one C 1 -C 4 alcohol from syngas, the method comprising:
(a) providing a reactor;
(b) providing a first catalyst composition comprising cobalt, molybdenum, sulfur, and a base promoter, wherein at least some of said cobalt and some of said sulfur are present as a cobalt-sulfur association having a first molar ratio of sulfur to cobalt, calculated by assuming all molybdenum is present as MoS 2 ;
(c) activating said first catalyst composition by contact with a stream comprising syngas, under suitable conditions for catalyst activation, thereby producing a second catalyst composition having a second molar ratio of sulfur to cobalt; and
(d) flowing syngas into said reactor at conditions effective to produce at least one C 1 -C 4 alcohol,
wherein said second molar ratio of sulfur to cobalt is lower than said first molar ratio of sulfur to cobalt.
2. The method of claim 1 , wherein said first molar ratio of sulfur to cobalt is at least 1.2.
3. The method of claim 1 , wherein said second molar ratio of sulfur to cobalt is 1.5 or less.
4. The method of claim 3 , wherein said second molar ratio of sulfur to cobalt is 0.5 or less.
5. The method of claim 1 , wherein said first molar ratio of sulfur to cobalt is at least 2 and said second molar ratio of sulfur to cobalt is 1.4 or less.
6. The method of claim 1 , wherein said activating step (c) is performed within said reactor provided in step (a).
7. The method of claim 1 , wherein a first amount of total cobalt contained in said first catalyst composition is capable of leaching into a 3N HCl solution, a second amount of total cobalt contained in said second catalyst composition is capable of leaching into a 3N HCl solution, and said second amount of cobalt is greater than said first amount of cobalt.
8. The method of claim 7 , wherein said first amount of total cobalt capable of leaching into a 3N HCl solution is less than about 10%.
9. The method of claim 7 , wherein said second amount of total cobalt capable of leaching into a 3N HCl solution is greater than about 40%.
10. The method of claim 7 , wherein said first amount of total cobalt capable of leaching into a 3N HCl solution is less than about 10% and wherein said second amount of total cobalt capable of leaching into a 3N HCl solution is greater than about 40%.
11. A method of producing at least one C 1 -C 4 alcohol from syngas, the method comprising:
(a) providing a reactor including a catalyst composition comprising cobalt, molybdenum, and sulfur, wherein at least some of said cobalt and some of said sulfur are present as a cobalt-sulfur association having a molar ratio of sulfur to cobalt (S:Co), calculated by assuming all molybdenum is present as MoS 2 ;
(b) flowing syngas into said reactor at conditions effective to produce at least one C 1 -C 4 alcohol; and
(c) injecting additional sulfur, or a compound containing sulfur, into said reactor, in an amount that is sufficient to maintain at least some of said cobalt in a sulfided state, and is further sufficient to maintain said molybdenum in a completely sulfided state.
12. The method of claim 11 , wherein said molar ratio S:Co is controlled to between about 0.1 and about 4.
13. The method of claim 12 , wherein said molar ratio S:Co is controlled to a ratio of at least 1.
14. The method of claim 11 , wherein said additional sulfur injected in step (c) is contained in one or more compounds selected from the group consisting of elemental sulfur, hydrogen sulfide, dimethyl disulfide, methylthiol, ethylthiol, cysteine, cystine, methionine, potassium disulfide, cesium disulfide, and sodium disulfide.
15. A composition for catalyzing the conversion of syngas into products comprising at least one C 1 -C 4 alcohol, said composition comprising sulfur, a first element or plurality of elements E1, and a second element or plurality of elements E2, wherein:
E1 is cobalt and/or nickel;
E2 is molybdenum and/or tungsten;
at least some of E1 and some of said sulfur are present as an E1-sulfur association; and
the molar ratio of sulfur to E1 (S:E1) in said association is at least 1.2,
said molar ratio S:E1 calculated after assigning some of said sulfur to E2 by assuming all E2 is present in said composition as E2S 2 .
16. The composition of claim 15 , wherein said molar ratio S:E1 is at least 1.5.
17. The composition of claim 15 , wherein said sulfur is present in a total amount of at least 30 wt % of said composition.
18. The composition of claim 15 , wherein said sulfur includes elemental sulfur in an amount of at least 100 ppm of said composition.
19. The composition of claim 15 , wherein said molar ratio of said E2 to said E1 is from about 1.5 to about 8.
20. The composition of claim 15 , further comprising one or more base promoters selected from the group consisting of potassium, rubidium, cesium, barium, strontium, scandium, yttrium, lanthanum, cerium, and any combinations thereof.