Low energy process to produce a hydrophobic oil from biomass pyrolysis liquids
Abstract
Described is a novel process for fractionating biomass pyrolysis oil quantitatively into energy dense hydrophobic aromatic fraction and water-soluble organics in an economical and energy efficient manner. Using the concepts of solvents and anti-solvent behaviors to separate the pyrolysis oil, which is an emulsion, a method utilizing minimal quantities of solvents and water is proposed, by comparison with the existing methods to isolate the hydrophobic aromatic fraction, there is a volume reduction of greater than 50:1. Additionally, there is a significant time saving over the 24 hours for the accepted method as a solvent, and the anti-solvent system is spontaneous.
Claims
exact text as granted — not AI-modified1 - 18 . (canceled)
19 . A process comprising:
fractionating pyrolysis oil to yield:
an organic phase comprising hydrophobic aromatics, and
an aqueous phase comprising water soluble organics; and
extracting the aqueous phase with an organic solvent to yield:
a fraction that is soluble in the organic solvent, and
a fraction that is insoluble in the organic solvent.
20 . The process according to claim 19 , wherein the extracting comprises:
combining the aqueous phase and the organic solvent to yield a mixture; agitating the mixture; and allowing the mixture to settle.
21 . The process according to claim 19 , further comprising distilling the fraction that is soluble in the organic solvent to remove the organic solvent, thereby yielding a product.
22 . The process according to claim 21 , wherein the product comprises phenolic monomers.
23 . The process according to claim 19 , further comprising:
extracting the fraction that is insoluble in the organic solvent with an additional organic solvent to yield:
a fraction that is soluble in the additional organic solvent, and
a fraction that is insoluble in the additional organic solvent.
24 . The process according to claim 23 , further comprising distilling the fraction that is insoluble in the additional organic solvent to remove water, thereby yielding a product.
25 . The process according to claim 23 , wherein the product comprises pyrolytic sugars.
26 . The process according to claim 23 , further comprising removing the additional organic solvent from the fraction that is soluble in the additional organic solvent.
27 . The process according to claim 23 , further comprising:
combining the fraction that is soluble in the organic solvent and the fraction that is soluble in the additional organic solvent to yield a mixture.
28 . The process according to claim 27 , further comprising distilling the mixture to remove the organic solvent and the additional organic solvent, thereby yielding a product.
29 . The process according to claim 28 , wherein the product comprises phenolics.
30 . The process according to claim 23 , further comprising:
combining the fraction that is soluble in the organic solvent, the fraction that is soluble in the additional organic solvent, and the organic phase to yield a mixture.
31 . The process according to claim 30 , further comprising distilling the mixture to remove the organic solvent, the additional organic solvent, and water thereby yielding a product.
32 . The process according to claim 31 , wherein the product comprises the hydrophobic aromatics.
33 . The process according to claim 23 , wherein extracting the fraction that is insoluble in the organic solvent with the additional organic solvent comprises:
combining the fraction that is insoluble in the organic solvent and the additional organic solvent to yield a mixture; and allowing the mixture to settle.
34 . The process according to claim 19 , wherein the organic solvent is diethyl ether.
35 . The process according to claim 34 , wherein the additional organic solvent is dichloromethane.
36 . The process according to claim 19 , wherein the organic solvent is butyl acetate.
37 . The process according to claim 36 , wherein the additional organic solvent is butyl acetate.
38 . A process comprising:
fractionating pyrolysis oil to yield:
an organic phase comprising hydrophobic aromatics, and
an aqueous phase comprising water soluble organics;
extracting the aqueous phase with diethyl ether to yield:
a diethyl ether-soluble fraction, and
a diethyl ether-insoluble fraction;
extracting the diethyl ether-insoluble fraction with dichloromethane to yield:
a dichloromethane-soluble fraction, and
a dichloromethane-insoluble fraction;
distilling the dichloromethane-insoluble fraction to remove water, thereby yielding pyrolytic sugars; distilling the diethyl ether-soluble fraction and the dichloromethane-soluble fraction to remove the diethyl ether and the dichloromethane, thereby yielding phenolic monomers.
39 . A process comprising:
fractionating pyrolysis oil to yield:
an organic phase comprising hydrophobic aromatics, and
an aqueous phase comprising water soluble organics;
extracting the aqueous phase with butyl acetate to yield:
a first butyl acetate-soluble fraction, and
a first butyl acetate-insoluble fraction;
extracting the first butyl acetate-insoluble fraction with additional butyl acetate to yield:
a second butyl acetate-soluble fraction, and
a second butyl acetate-insoluble fraction;
distilling the second butyl acetate-soluble fraction to remove water, thereby yielding pyrolytic sugars; combining the first butyl acetate-soluble fraction and the second butyl acetate-soluble fraction with the organic phase to yield a mixture; and distilling the mixture to remove the butyl acetate and water, thereby yielding the hydrophobic aromatics.Join the waitlist — get patent alerts
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