US2017145445A1PendingUtilityA1
Process and Systems for the Fermentative Production of Alcohols
Assignee: BUTAMAX ADVANCED BIOFUELS LLCPriority: Sep 12, 2012Filed: Oct 14, 2016Published: May 25, 2017
Est. expirySep 12, 2032(~6.2 yrs left)· nominal 20-yr term from priority
Inventors:Stephane Francois BazzanaJames Timothy CroninMichael Charles GradyDavid J. LoweBrian Michael RoeschJoseph J. ZaherRaymond Richard Zolandz
C12P 7/16C12M 41/48C12M 33/00C12M 47/10C12M 43/02C12M 21/12C12P 7/10C12M 41/26C12P 2203/00C12P 7/14Y02E50/10C11B 1/10C11B 1/025
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Claims
Abstract
The present invention relates to the fermentative production of alcohols including ethanol and butanol, and processes for improving alcohol fermentation employing in situ product removal methods.
Claims
exact text as granted — not AI-modified1 - 21 . (canceled)
22 . A method for recovering a product alcohol from a fermentation broth comprising
providing a fermentation broth comprising a microorganism, wherein the microorganism produces product alcohol in a fermentor; providing a feedstock slurry comprising fermentable carbon source, undissolved solids, oil, and water; separating the feedstock slurry whereby (i) an aqueous solution comprising fermentable carbon source, (ii) a wet cake comprising solids, and (iii) an oil are formed; adding the aqueous solution to the fermentation broth; contacting the fermentation broth with at least one extractant; and recovering the product alcohol.
23 . The method of claim 22 , wherein the oil is hydrolyzed to form fatty acids.
24 . The method of claim 23 , wherein the fermentation broth is contacted with the fatty acids.
25 . The method of claim 23 , wherein the oil is hydrolyzed by an enzyme.
26 . The method of claim 25 , wherein the enzyme is one or more lipases or phospholipases.
27 . The method of claim 22 , wherein the feedstock slurry is generated by hydrolysis of feedstock.
28 . The method of claim 27 , wherein feedstock is selected from rye, wheat, corn, cane, barley, cellulosic or lignocellulosic material, or combinations thereof.
29 . The method of claim 22 , wherein the feedstock slurry is separated by decanter bowl centrifugation, three-phase centrifugation, disk stack centrifugation, filtering centrifugation, decanter centrifugation, filtration, vacuum filtration, beltfilter, pressure filtration, filtration using a screen, screen separation, grating, porous grating, flotation, hydroclone, filter press, screwpress, gravity settler, vortex separator, or combination thereof.
30 . The method of claim 22 , wherein separating the feedstock is a single step process.
31 . The method of claim 22 , wherein the wet cake is combined with the aqueous solution.
32 . The method of claim 22 , further comprising contacting the aqueous solution with a catalyst converting oil in the aqueous solution to fatty acids.
33 . The method of claim 32 , wherein the aqueous solution and fatty acids are added to the fermentation broth.
34 . The method of claim 32 , wherein the catalyst is deactivated.
35 . A system comprising
one or more fermentors comprising:
an inlet for receiving feedstock slurry; and
an outlet for discharging fermentation broth comprising product alcohol; and
one or more extractors comprising:
a first inlet for receiving the fermentation broth;
a second inlet for receiving extractant;
a first outlet for discharging a lean fermentation broth; and
a second outlet for discharging a rich extractant.
36 . The system of claim 35 , further comprising
one or more liquefaction units; one or more separation means; and optionally one or more wash systems.
37 . The system of claim 36 , wherein the separation means is selected from decanter bowl centrifugation, three-phase centrifugation, disk stack centrifugation, filtering centrifugation, decanter centrifugation, filtration, vacuum filtration, belt filter, pressure filtration, membrane filtration, filtration using a screen, screen separation, grating, porous grating, flotation, hydroclone, filter press, screwpress, gravity settler, vortex separator, and combinations thereof.
38 . The system of claim 35 , wherein the system further comprises on-line measurement devices.
39 . The system of claim 38 , wherein the on-line measurement devices are selected from particle size analyzers, Fourier transform infrared spectroscopes, near-infrared spectroscopes, Raman spectroscopes, high pressure liquid chromatography, viscometers, densitometers, tensiometers, droplet size analyzers, pH meters, dissolved oxygen probes, or combinations thereof.Cited by (0)
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