Upgrading of fusel oils over doped alumina
This present disclosure relates to a catalytic process for upgrading crude and/or refined fusel oil mixtures to higher value renewable 2-methyl-2-butene, via novel doped alumina catalysts. It was found that passing a vaporized stream of crude and/or refined fusel oils over doped alumina catalysts provides renewable 2-methyl-2-butene in high yields in a single step. Subsequent downstream purification of the reactor effluent results in a renewable 2-methyl-2-butene at competitive price and quality to fossil fuel derived 2-methyl-2-butene.
1. A process for converting fusel oils to renewable chemicals, the process comprising:
contacting a feed stream comprising the fusel oils with an alumina catalyst at a temperature from about 200° C. to about 500° C., and a weight hourly space velocity (WHSV) of at least 1.0, wherein the alumina catalyst comprises one or more of zirconium (Zr), titanium (Ti), silicon (Si), or fluorine (F) in neutral or ionic form; and
forming the renewable chemicals, wherein the renewable chemicals comprise 2-methyl-2-butene in an amount of at least 50 wt. % yield;
wherein the fusel oils comprise ethanol, isobutanol, 3-methyl-1-butanol, and 2-methyl-1-butanol, and wherein the 3 methyl-1-butanol is present in the fusel oils in an amount of about 40 wt. % to about 70 wt. %.
2. The process of claim 1 , wherein the fusel oils further comprise propanol, isopropanol, 1-butanol, 2 butanol, tert-butanol, pentanol, 2,2-dimethyl-1-propanol, 3-pentanol, 2-pentanol, 3-methyl-2-butanol, 2-methyl-2-butanol, or any combination thereof.
3. The process of claim 1 , wherein the fusel oils further comprise water.
4. The process of claim 1 , wherein the fusel oils comprise crude fusel oils, refined fusel oils, or a combination thereof.
5. The process of claim 1 , wherein the ethanol is present in the fusel oils in an amount of about 1 wt. % to about 15 wt. %.
6. The process of claim 1 , wherein the isobutanol is present in the fusel oils in an amount of about 2 wt. % to about 25 wt. %.
7. The process of claim 1 , wherein the fusel oils further comprise a recycled feed stream.
8. The process of claim 1 , wherein the renewable chemicals further comprise one or more of 3-methyl-1-butene, 2-methyl-1-butene, C 2 -C 5 olefins, C 5 olefins, or C 2 -C 3 olefins.
9. The process of claim 1 , wherein the renewable chemicals further comprise 2-methyl-1-butene, which is present in an amount of at least 15 wt. % yield.
10. The process of claim 1 , wherein the renewable chemicals further comprise 2-methyl-1-butene, and wherein a ratio of 2-methyl-2-butene to 2-methyl-1-butene by wt. % is from about 2:1 to about 5:1.
11. The process of claim 1 , wherein the renewable chemicals further comprise 3-methyl-1-butene, and wherein a ratio of 2-methyl-2-butene to 3-methyl-1-butene by wt. % is from about 10:1 to about 15:1.
12. The process of claim 1 , wherein a ratio of 2-methyl-1-butene to 3-methyl-1-butene by wt. % is from about 5:1 to about 10:1.
13. The process of claim 1 , wherein the alumina catalyst is a γ-alumina.
14. The process of claim 1 , wherein the one or more of Zr, Ti, Si, or F is present in the alumina catalyst in an amount of about 3 wt. % to about 15 wt. %.
15. The process of claim 1 wherein the alumina catalyst is regenerated in-situ via air.
16. The process of claim 15 , wherein the alumina catalyst is regenerated at a temperature from about 400° C. to about 600° C.
17. The process of claim 1 , wherein contacting the feed stream at a pressure of 0 psig to about 100 psig.
18. A process for converting fusel oils to renewable chemicals, the process comprising:
contacting a feed stream comprising fusel oils with an alumina catalyst at a temperature of about 420° C., and a weight hourly space velocity (WHSV) of about 2.5, wherein the alumina catalyst is γ-alumina and comprises Zirconium (IV); and
forming the renewable chemicals, wherein the renewable chemicals are C 2 -C 5 olefins and further comprises 2-methyl-2-butene in an amount of about 60 wt. % yield;
wherein the fusel oils comprise ethanol, isobutanol, 3-methyl-1-butanol, and 2-methyl-1-butanol, and wherein the 3-methyl-1-butanol is present in the fusel oils in an amount of about 40 wt. % to about 70 wt. %.