US2015307904A1PendingUtilityA1

Methods for the Economical Production of Biofuel from Biomass

Assignee: GEVO INCPriority: Oct 31, 2007Filed: Nov 21, 2014Published: Oct 29, 2015
Est. expiryOct 31, 2027(~1.3 yrs left)· nominal 20-yr term from priority
C12P 7/04C10L 2200/0469C10L 1/02C12P 7/16C10L 2290/26C12Y 106/01002C10G 2300/1014Y02P30/20C12Y 302/01003C07K 14/245C10G 1/04C12N 9/0006C12N 9/2414C10G 2300/4025Y02E50/10C12N 9/2434C12Y 302/01001C12N 9/2417C12P 7/24C12P 7/62C12N 9/0036C12N 9/2428
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Claims

Abstract

Methods for producing a biofuel are provided. Also provided are biocatalysts that convert a feedstock to a biofuel.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A method of making a biofuel, comprising:
 providing a biocatalyst selected to convert a feedstock into the biofuel at a yield of at least 80 percent of theoretical, a productivity of at least 0.75 grams biofuel per liter per hour, and a titer equivalent to a lower one of (i) a solubility limit of the biofuel in water under the process conditions and (ii) 2% (w/w) of the biofuel in water;   providing the biocatalyst selected to have at least two properties from a. to l. as follows:   a. the biocatalyst selected to convert at least two sugars, including each of (i) at least one of a six-carbon sugar and a six-carbon sugar oligomer, and (ii) at least one five-carbon sugar, derived from at least one of starch, cellulose, hemicellulose, and pectin into the biofuel;   b. the biocatalyst exhibiting a level of endotoxin toxicity or exotoxin toxicity, wherein the level of endotoxin or exotoxin toxicity in the biocatalyst has a median lethal dose (LD50) of at least 1000-fold more than the amount present in 1 kilogram of at least one of a DDG and a DDGS product;   c. the biocatalyst containing no DNA markers;   d. the biocatalyst operable to produce the biofuel free of byproducts that would require additional processing steps for removal from the biofuel;   e. the biocatalyst operable at a pH value between about 2 to 10 to produce the biofuel;   f. the biocatalyst selected to have a recoverable productivity from a sudden change of about 1 pH unit from the first pH;   g. the biocatalyst operable within a temperature range of about 20° C. to 60° C. to produce the biofuel;   h. the biocatalyst selected to have a recoverable productivity from a sudden change of about 5° C. from the first temperature;   i. the biocatalyst operable in a medium comprising feedstock;   j. the biocatalyst selected to have a growth rate of at least 0.2 per hour;   k. providing a facultative anaerobic biocatalyst operable at dissolved oxygen concentrations across a range of about 0% to about 0.01% air saturation to produce the biofuel; and   l. providing an anaerobic biocatalyst selected to have a productivity that recovers from an exposure to more than 1% air saturation that lasts for up to three hours;   and cultivating the biocatalyst in a culture medium until a recoverable quantity of the biofuel is produced;   and recovering the biofuel.

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