Conversion of carbohydrates to hydrocarbons
View Patent ↗Materials and processes for the conversion of carbohydrates and polyols to gasoline boiling range hydrocarbons. Carbohydrates and polyols are reacted in the presence of modified zeolite catalysts to form a reaction product containing non-aromatic and aromatic gasoline boiling range hydrocarbons.
1. A method of converting carbohydrates to polyols and gasoline boiling range hydrocarbons comprising:
a) contacting a zinc-platinum or cobalt-molybdenum impregnated zeolite catalyst (ZnPt-zeolite or CoMo-zeolite) with a carbohydrate or polyol;
b) reacting said carbohydrate or polyol on said catalyst to produce polyols and hydrocarbons; and
c) separating the polyols and hydrocarbons,
wherein said hydrocarbons are in the gasoline boiling range between approximately −20° C. and 220° C.
2. The method of claim 1 , wherein said carbohydrate is selected from the group consisting of starches, polysaccharides, monosaccharides, dextrose, mannose, galactose, fructose, sucrose, and combinations thereof.
3. The method of claim 1 , wherein said polyol is selected from the group consisting of maltitol, sorbitol, xylitol, isomalt and/or isomers and/or combinations thereof.
4. The method of claim 1 , wherein said zeolite catalyst is selected from the group consisting of HZSM-5, ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-35, ZSM-38, MFI, and pentasil.
5. The method of claim 1 , wherein said reaction (b) comprises a hydrogen co-feed gas.
6. The method of claim 1 , wherein said hydrocarbon is a hydrocarbon with C1, C2, C3, C4, C5, C6, C7, C8, C9, C10, C11 or C12 hydrocarbons.
7. The method of claim 1 , wherein said hydrocarbon has a boiling range selected from the group consisting of between approximately minus 20° C. to 220° C., between approximately minus 20° C. to 120° C., between approximately minus 20° C. to 196° C., between approximately 35° C. to 160° C., and between approximately 140° C. to 220° C.
8. The method of claim 1 , wherein said hydrocarbon is selected from the group consisting of alkanes, cycloalkanes, alkenes, and aromatic hydrocarbons.
9. The method of claim 8 , wherein said hydrocarbon is further selected from the group consisting of toulene, xylene, pentane, trimethylbenzenes, benzene, butane, ethylbenzene, heptane, cyclohexane, hexane, octane, naphthalene, isopentane, and styrene.
10. A method of converting carbohydrates to gasoline boiling range hydrocarbons comprising:
a) contacting a zinc-platinum or cobalt-molybdenum impregnated zeolite (ZnPt-zeolite or CoMo-zeolite) catalyst with a carbohydrate;
b) reacting said carbohydrate on said catalyst to produce hydrocarbons; and
c) purifying the hydrocarbons from the reaction (b),
wherein said hydrocarbons are in the gasoline boiling range between approximately −20° C. and 220° C.
11. The method of claim 10 , wherein said carbohydrate is selected from the group consisting of starches, polysaccharides, monosaccharides, dextrose, mannose, galactose, fructose, sucrose, and combinations thereof.
12. The method of claim 10 , wherein said zeolite catalyst is selected from the group consisting of HZSM-5, ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-35, ZSM-38, MFI, and pentasil.
13. The method of claim 10 , wherein said reaction (b) comprises a hydrogen co-feed gas.
14. The method of claim 10 , wherein said hydrocarbon is a hydrocarbon with C1, C2, C3, C4, C5, C6, C7, C8, C9, C10, C11 or C12 hydrocarbons.
15. The method of claim 10 , wherein said hydrocarbon has a boiling range selected from the group consisting of between approximately minus 20° C. to 220° C., between approximately minus 20° C. to 120° C., between approximately minus 20° C. to 196° C., between approximately 35° C. to 160° C., and between approximately 140° C. to 220° C.
16. The method of claim 10 , wherein said hydrocarbon is selected from the group consisting of alkanes, cycloalkanes, alkenes, and aromatic hydrocarbons.
17. The method of claim 16 , wherein said hydrocarbon is further selected from the group consisting of toluene, xylene, pentane, trimethylbenzenes, benzene, butane, ethylbenzene, heptane, cyclohexane, hexane, octane, naphthalene, isopentane, and styrene.
18. A method of converting polyols to gasoline boiling range hydrocarbons comprising:
a) contacting a zinc-platinum or cobalt-molybdenum impregnated zeolite catalyst with a polyol;
b) reacting said polyol on said catalyst to produce hydrocarbons; and
c) purifying the hydrocarbons from the reaction (b),
wherein said hydrocarbons are in the gasoline boiling range between approximately −20° C. and 220° C.
19. The method of claim 18 , wherein said polyol is selected from the group consisting of maltitol, sorbitol, xylitol, isomalt and/or isomers and/or combinations thereof.
20. The method of claim 18 , wherein said zeolite catalyst is selected from the group consisting of HZSM-5, ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-35, ZSM-38, MFI, and pentasil.
21. The method of claim 18 , wherein said reaction (b) comprises a hydrogen co-feed gas.
22. The method of claim 18 , wherein said hydrocarbon is a hydrocarbon with C2, C3, C4, C5, C6, C7, C8, C9, C10, C11 or C12 hydrocarbons.
23. The method of claim 18 , wherein said hydrocarbon has a boiling range selected from the group consisting of between approximately minus 20° C. to 220° C., between approximately minus 20° C. to 120° C., between approximately minus 20° C. to 196° C., between approximately 35° C. to 160° C., and between approximately 140° C. to 220° C.
24. The method of claim 18 , wherein said hydrocarbon is selected from the group consisting of alkanes, cycloalkanes, alkenes, and aromatic hydrocarbons.
25. The method of claim 24 , wherein said hydrocarbon is further selected from the group consisting of toluene, xylene, pentane, trimethylbenzenes, benzene, butane, ethylbenzene, heptane, cyclohexane, hexane, octane, naphthalene, isopentane, and styrene.
26. A method of converting polyols to hydrocarbons comprising:
a) contacting a leached zeolite catalyst impregnated with zinc, cobalt, molybdenum, platinum or combinations thereof,
b) reacting said polyol on said catalyst to produce hydrocarbons, and
c) purifying hydrocarbons from the reaction,
wherein said reaction temperature is between 400 and 550° C., said reaction pressure is between 1 and 250 psig, and said polyol flow rate is between approximately 0.1 and 5 ml/hr/g catalyst.
27. The method of claim 26 , wherein said polyol is co-fed with between approximately 1 and 2.5 ml/hr/mg catalyst liquid co-feed.
28. The method of claim 27 , wherein said liquid co-feed is methanol or pentane.
29. The method of claim 26 , wherein said polyol is an aqueous solution between 30 and 95% sorbitol.
30. The method of claim 26 , wherein said reaction temperature is approximately 450° C., said reaction pressure is approximately 200 psig, and said polyol is 1.3 ml/hr 70% sorbitol per gram catalyst.
31. The method of claim 30 , wherein said reaction comprises a co-feed of 1.5 ml/hr methanol per gram catalyst.
32. The method of claim 26 , wherein said reaction temperature is approximately 500° C., said pressure is approximately 14 psig, and said polyol is approximated 3 ml/hr 50% sorbitol per gram catalyst.
33. The method of claim 32 , wherein said reaction comprises a co-feed of 1.6 ml/hr isopentane per gram catalyst.
34. The method of claim 26 , wherein said polyol is selected from the group consisting of maltitol, sorbitol, xylitol, isomalt and/or isomers and/or combinations thereof.
35. The method of claim 26 , wherein said zeolite catalyst is selected from the group consisting of HZSM-5, ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-35, ZSM-38, MFI, and pentasil.
36. The method of claim 26 , wherein said reaction (b) comprises a hydrogen co-feed gas.
37. The method of claim 26 , wherein said hydrocarbon is a hydrocarbon with C2, C3, C4, C5, C6, C7, C8, C9, C10, C11 or C12 hydrocarbons.
38. The method of claim 26 , wherein said hydrocarbon has a boiling range selected from the group consisting of between approximately minus 20° C. to 220° C., between approximately minus 20° C. to 120° C., between approximately minus 20° C. to 196° C., between approximately 35° C. to 160° C., and between approximately 140° C. to 220° C.
39. The method of claim 26 , wherein said hydrocarbon is selected from the group consisting of alkanes, cycloalkanes, alkenes, and aromatic hydrocarbons.
40. The method of claim 39 , wherein said hydrocarbon is further selected from the group consisting of toluene, xylene, pentane, trimethylbenzenes, benzene, butane, ethylbenzene, heptane, cyclohexane, hexane, octane, naphthalene, isopentane, and styrene.