Processing biomass
US-2017159077-A1 · Jun 8, 2017 · US
US10087471B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10087471-B2 |
| Application number | US-201615092829-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 7, 2016 |
| Priority date | Apr 9, 2015 |
| Publication date | Oct 2, 2018 |
| Grant date | Oct 2, 2018 |
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The present disclosure relates to a hydrolysate of a mixture of lignocellulosic biomass and seaweed biomass. By mixing seaweed biomass with lignocellulosic biomass and then preparing a hydrolysate, lignocellulosic biomass-derived acetic acid is consumed together with seaweed biomass-derived mannitol. As a result, high sugar productivity can be maintained while reducing fermentation inhibitors. Because the present disclosure can solve the problem of lignocellulosic biomass of decreased fermentation efficiency due to lignocellulose-derived fermentation inhibitors and the problem of seaweed biomass of very low productivity in spite of long fermentation time, the hydrolysate according to the present disclosure may be used to produce biofuels and biochemicals economically.
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What is claimed is: 1. A hydrolysate for use in fermentation by microorganisms, the hydrolysate being a hydrolysate of a mixture of seaweed biomass and lignocellulosic biomass, wherein the hydrolysate is configured to generate lignocellulosic biomass-derived acetic acid and seaweed biomass-derived mannitol when fermented together, and the generated acetic acid and mannitol are consumed when the hydrolysate is fermented, wherein the seaweed biomass is one or more selected from red algae, brown algae, and green algae. 2. The hydrolysate according to claim 1 , wherein the seaweed biomass is brown algae biomass. 3. The hydrolysate according to claim 1 , wherein the hydrolysate comprises fermentation inhibitors naturally present without external removal of fermentation inhibitors in an amount of at least 50 wt % less than an amount of fermentation inhibitors naturally present without external removal of fermentation inhibitors in a lignocellulosic biomass hydrolysate based on the total volume of the hydrolysate, when the amount of the mixture of seaweed biomass and lignocellulosic biomass is the same as the lignocellulosic biomass of the lignocellulosic biomass hydrolysate, and the fermentation inhibitors comprise one or more of phenolic compounds and furan-based compounds. 4. The hydrolysate according to claim 1 , wherein the mixture of seaweed biomass and lignocellulosic biomass has a weight ratio of seaweed biomass and lignocellulosic biomass of 9:1-1:9. 5. The hydrolysate according to claim 1 , wherein the hydrolysate is configured to generate fermentation inhibitors in an amount of at least 80 wt % less than an amount of fermentation inhibitors generated by a lignocellulosic biomass hydrolysate based on the total volume of the hydrolysate, when the amount of the mixture of seaweed biomass and lignocellulosic biomass is the same as the lignocellulosic biomass of the lignocellulosic biomass hydrolysate. 6. The hydrolysate according to claim 3 , wherein the fermentation inhibitor comprises one or more selected from: one or more phenolic compound selected from a group consisting of ferulic acid, coumaric acid, benzoic acid, syringic acid, vanillic acid, vanillin, 4-hydroxybenzoic acid, 4-hydroxybenzaldehyde and syringaldehyde; and one or more furan-based compound selected from a group consisting of furan, furfural and 5-hydroxymethylfurfural (5-HMF). 7. The hydrolysate according to claim 1 , wherein the hydrolysate of a mixture of seaweed biomass and lignocellulosic biomass comprises 75-100 wt % of sugar as compared to a lignocellulosic biomass hydrolysate based on the total volume of the hydrolysate when the amount of the mixture of seaweed biomass and lignocellulosic biomass is the same as the lignocellulosic biomass of the lignocellulosic biomass hydrolysate. 8. The hydrolysate according to claim 7 , wherein the sugar is one or more selected from a group consisting of a monosaccharide; a disaccharide; and one or more and a polysaccharide, wherein the monosaccharide is one or more selected from a group consisting of glucose, galactose, mannose, rhamnose, xylose and arabinose, wherein the disaccharide is cellobiose, and wherein the polysaccharide is one or more selected from a group consisting of mannitol, alginic acid and laminaran. 9. A hydrolysate for use in fermentation by microorganisms, the hydrolysate being a mixture of a hydrolysate of seaweed biomass and a hydrolysate of lignocellulosic biomass, wherein the hydrolysate mixture comprises lignocellulosic biomass-derived acetic acid and seaweed biomass-derived mannitol, wherein the hydrolysate mixture comprises the acetic acid in a proportion to be consumed together with the mannitol when the hydrolysate mixture is fermented, wherein the seaweed biomass is one or more selected from red algae, brown algae, and green algae. 10. The hydrolysate according to claim 9 , wherein the seaweed biomass is brown algae biomass. 11. The hydrolysate according to claim 9 , wherein the mixture of a hydrolysate of seaweed biomass and a hydrolysate of lignocellulosic biomass is configured to generate fermentation inhibitors in an amount of at least 50 wt % less than an amount of fermentation inhibitors generated by a lignocellulosic biomass hydrolysate based on the total volume of the hydrolysate, when the amount of the mixture of seaweed biomass and lignocellulosic biomass is the same as the lignocellulosic biomass of the lignocellulosic biomass hydrolysate, and the fermentation inhibitors comprise one or more of phenolic compounds and furan-based compounds. 12. The hydrolysate according to claim 9 , wherein the mixture of a hydrolysate of seaweed biomass and a hydrolysate of lignocellulosic biomass has a weight ratio of seaweed biomass and lignocellulosic biomass of 9:1-1:9. 13. The hydrolysate according to claim 9 , wherein the mixture of a hydrolysate of seaweed biomass and a hydrolysate of lignocellulosic biomass comprises fermentation inhibitors naturally present without external removal of fermentation inhibitors in an amount of at least 80 wt % less than an amount of fermentation inhibitors naturally present without external removal of fermentation inhibitors in a lignocellulosic biomass hydrolysate based on the total volume of the hydrolysate, when the amount of the mixture of seaweed biomass and lignocellulosic biomass is the same as the lignocellulosic biomass of the lignocellulosic biomass hydrolysate. 14. The hydrolysate according to claim 11 , wherein the fermentation inhibitor comprises one or more selected from: one or more phenolic compound selected from a group consisting of ferulic acid, coumaric acid, benzoic acid, syringic acid, vanillic acid, vanillin, 4-hydroxybenzoic acid, 4-hydroxybenzaldehyde and syringaldehyde; and one or more furan-based compound selected from a group consisting of furan, furfural and 5-hydroxymethylfurfural (5-HMF). 15. The hydrolysate according to claim 9 , wherein the mixture of a hydrolysate of seaweed biomass and a hydrolysate of lignocellulosic biomass comprises 75-100 wt % of a sugar as compared to a lignocellulosic biomass hydrolysate when the amount of the mixture of seaweed biomass and lignocellulosic biomass is the same as the lignocellulosic biomass of the lignocellulosic biomass hydrolysate. 16. The hydrolysate according to claim 15 , wherein the sugar is one or more selected from a monosaccharide; a disaccharide; and a polysaccharide, wherein the monosaccharide is one or more selected from a group consisting of glucose, galactose, mannose, rhamnose, xylose, and arabinose, wherein the disaccharide is cellobiose, and wherein the polysaccharide is one or more selected from a group consisting of mannitol, alginic acid and laminaran.
Cross-Sectional Technologies · mapped topic
Cross-Sectional Technologies · mapped topic
Disaccharides · CPC title
Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source · CPC title
Monosaccharides (2-ketogulonic acid C12P7/60) · CPC title
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