Thermal pyoil to a gas fed cracker furnace
US-2024309276-A1 · Sep 19, 2024 · US
US9856427B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9856427-B2 |
| Application number | US-201214123064-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 26, 2012 |
| Priority date | May 27, 2011 |
| Publication date | Jan 2, 2018 |
| Grant date | Jan 2, 2018 |
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The present disclosure provides methods to produce ketones suitable for use as fuels and lubricants by catalytic conversion of an acetone-butanol-ethanol (ABE) fermentation product mixture that can be derived from biomass.
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What is claimed is: 1. A method of producing two or more compounds of Formula I, wherein each R 1 and R 2 is independently an optionally substituted member selected from the group consisting of alkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, and arylalkyl, wherein the method comprises: a) contacting biomass or sugars with a fermentation host to produce a fermentation product mixture, wherein the fermentation product mixture comprises acetone and two or more optionally substituted primary alcohols; b) combining the fermentation product mixture with metal-based catalyst in the presence of base, wherein the metal-based catalyst comprises rhodium, palladium, iridium, or platinum, or a combination thereof; and c) producing two or more compounds of Formula I, wherein at least two of the two or more compounds of Formula I are double-alkylated. 2. The method of claim 1 , wherein each R 1 and R 2 is independently an optionally substituted C1-C20 alkyl. 3. The method of claim 1 , wherein the biomass or sugars and the fermentation host are further contacted with an extractant having one or more of the following properties: i) is non-toxic to Clostridium; ii) has partition coefficients for acetone and butanol equal to or greater than 1; and iii) has a partition coefficient for ethanol of less than 0.5. 4. The method of claim 3 , wherein the extractant is glyceryl tributyrate, glyceryl tripropionate, oleyl alcohol, polypropylene glycol, or a combination thereof. 5. The method of claim 1 , wherein the fermentation product mixture has less than 5 wt % water. 6. The method of claim 1 , wherein the fermentation product mixture comprises acetone, butanol, and ethanol. 7. The method of claim 1 , wherein the metal-based catalyst comprises palladium supported or tethered on a solid support. 8. The method of claim 1 , wherein the metal-based catalyst comprises Pd(OAc) 2 , Pd 2 (dba) 3 , Pd(OH) 2 /C, Pd/C, Pd/CaCO 3 , Pd/Alumina, or Pd-polyethylenimines on silica. 9. The method of claim 1 , wherein the base is K 3 PO 4 , KOH, Ba(OH) 2 .8H 2 O, K 2 CO 3 , KOAc, KH 2 PO 4 , Na 2 HPO 4 , pyridine, Et 3 N, or a combination thereof. 10. The method of claim 1 , wherein the two or more compounds of Formula I are produced at a temperature between 110° C. to 145° C. 11. The method of claim 1 , wherein the two or more compounds of Formula I are produced at a temperature between 140° C. to 220° C. 12. The method of claim 1 , wherein the yield of the two or more compounds of Formula I relative to the amount of acetone present in the fermentation product mixture is at least 10%. 13. The method of claim 1 , wherein the yield of the double-alkylated compounds of Formula I relative to the amount of acetone present in the fermentation product mixture is at least 10%. 14. The method of claim 13 , wherein the metal-based catalyst comprises Pd(OAc) 2 , Pd 2 (dba) 3 , Pd(OH) 2 /C, Pd/C, Pd/CaCO 3 , Pd/Alumina, Pd-polytheylenimines on silica, PtCl 2 (COD), [Rh(COD)Cl] 2 , or Pt/C.
Ketones · CPC title
Biofuels, e.g. bio-diesel · CPC title
Butanols · CPC title
Saturated compounds containing keto groups bound to acyclic carbon atoms · CPC title
essentially based on components consisting of carbon, hydrogen, and oxygen only · CPC title
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