Process to prepare levulinic acid
The invention describes processes to prepare levulinic acid, formic acid and/or hydroxymethyl furfural from various biomass materials.
1. A process to prepare levulinic acid comprising the steps:
a) heating an aqueous solution of a mineral acid to a temperature from about 60° C. to about 160° C. in a reactor, wherein the mineral acid is present from at least 20 percent by weight to about 80 percent by weight; and
b) adding a monosaccharide or di-saccharide to the heated aqueous acid in the reactor to form a reaction mixture at a rate such that the monosaccharide content of the reaction mixture remains less than or equal to about 5% by weight of the reaction mixture during the entire reaction, to provide levulinic acid.
2. The process of claim 1 , further comprising the step of combining the reaction mixture comprising levulinic acid with a phenolic or substituted phenolic extraction solvent to create an extraction phase and an aqueous raffinate phase, wherein levulinic acid and optionally, formic acid are in the extraction phase.
3. The process of claim 2 , wherein the phenolic or substituted phenolic extraction solvent is a phenol, an alkylphenol, a xylenol, a methoxyphenol, a cresol, a polydimethylsiloxane, a substituted alkyl phenol, a tertiary amine/alkyl phenol mixture, phenol/alkyl phenol blends with a C5-C36 hydrocarbon or C6-C12 aromatic hydrocarbons, 2-ethyl-hexanoic acid or perfluoro-octanoic acid or perfluoro-octanol or mixtures thereof.
4. The process of claim 3 , wherein the extraction solvent comprises phenol, 4-methoxyphenol, 2-methoxyphenol, 3-methoxyphenol, 2-sec-butyl phenol, 3-sec-butyl phenol, 4-sec-butyl phenol, 2-t-butyl phenol, 4-t-butyl phenol, 2,4-di-t-butyl phenol, 2,4-di-methoxyphenol, 2-methylphenol, 3-methylphenol, 4-methylphenol, 2,3-xylenol, 2, 4-xylenol, 2, 5-xylenol, 2, 6-xylenol, 3, 4-xylenol, or 3, 5-xylenol, 4-hexyl-resorcinol, butylated hydroxyl-toluene (BHT), 2,5-dimethoxyphenol, 3,5-dimethoxy phenol, 2,6-dimethoxy phenol, nonylphenol, or mixtures thereof.
5. The process of claim 2 , further comprising the step of subjecting the extraction phase to a base, an anion exchange resin, or water washing the extraction phase to reduce the amount of mineral acid present to less than or equal to 0.5 weight percent of the extraction phase.
6. The process of claim 2 , further comprising the step of treating the aqueous raffinate phase with an adsorbent, such as activated carbon or with a hydrocarbon solvent to decrease the amount of the extraction solvent from the raffinate phase.
7. A process to prepare levulinic acid comprising the steps:
a) providing a heated reaction mixture comprising a biomass, water and a mineral acid, at a temperature from about 60° C. to about 160° C., such that the monosaccharide content of the reaction mixture remains less than or equal to about 5% by weight of the reaction mixture during the entire reaction, to produce levulinic acid;
b) extracting levulinic acid from the reaction mixture with an extraction solvent in an extraction system, wherein the extracted levulinic acid and extraction solvent comprise an extraction phase;
c) recycling an aqueous raffinate recycle stream from the extraction vessel to the reactor wherein the recycle stream comprises the water, the mineral acid and less than or equal to 0.5 weight percent of the extraction solvent; and
d) distilling the extraction solvent such that the extraction solvent contains <1% mineral acid prior to recycling back to the extraction system.
8. The process of claim 7 , wherein the extraction solvent is a phenolic or substituted phenolic comprising phenol, an alkylphenol, a xylenol, a methoxyphenol, a cresol, a polydimethylsiloxane, a substituted alkyl phenol, a tertiary amine/alkyl phenol mixture, phenol/alkyl phenol blends with a C5-C36 hydrocarbon or C6-C12 aromatic hydrocarbons, 2-ethyl-hexanoic acid or perfluoro-octanoic acid or perfluoro-octanol or mixtures thereof.
9. The process of claim 8 , wherein the extraction solvent comprises phenol, 4-methoxyphenol, 2-methoxyphenol, 3-methoxyphenol, 2-sec-butyl phenol, 3-sec-butyl phenol, 4-sec-butyl phenol, 2-t-butyl phenol, 4-t-butyl phenol, 2,4-di-t-butyl phenol, 2,4-di-methoxyphenol, 2-methylphenol, 3-methylphenol, 4-methylphenol, 2,3-xylenol, 2, 4-xylenol, 2, 5-xylenol, 2, 6-xylenol, 3, 4-xylenol, or 3, 5-xylenol, 4-hexyl-resorcinol, butylated hydroxyl-toluene (BHT), 2,5-dimethoxyphenol, 3,5-dimethoxy phenol, 2,6-dimethoxy phenol, nonylphenol, or mixtures thereof.
10. The process of claim 7 , further comprising the step of subjecting the extraction phase to a base, an anion exchange resin, or water washing the extraction phase to reduce the amount of mineral acid present to less than or equal to 0.5 weight percent of the extraction phase.
11. The process of claim 7 , further comprising the step of treating the aqueous raffinate phase with an adsorbent, such as activated carbon or with a hydrocarbon solvent to decrease the amount of the extraction solvent from the raffinate phase.
12. The process of claim 7 , further comprising the step of washing char/solids with water to form a filtrate and combining the filtrate with the raffinate or contacting the filtrate with an extraction solvent.
13. The process of claim 7 , further comprising the step of recycling the extraction phase to a liquid extraction system.
14. The process of claim 7 , wherein step (a) is conducted in a batch.
15. The process of claim 7 , wherein the recycle step is conducted in a continuous manner.
16. The process of claim 7 , wherein the distillation step is conducted in a continuous manner.