Converting lignocellulosic biomass to glucose using a low temperature sulfur dioxide pretreatment
US-11299850-B2 · Apr 12, 2022 · US
US2022017928A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022017928-A1 |
| Application number | US-201817309080-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 9, 2018 |
| Priority date | Nov 9, 2018 |
| Publication date | Jan 20, 2022 |
| Grant date | — |
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A process for producing a fuel from a softwood. A feedstock containing softwood is pretreated, where the pretreating includes heating the feedstock in a pretreatment liquor containing sulfur dioxide and bisulfite salt. The heating is conducted between 110° C. and 160° C. The pretreatment liquor has a sulfur dioxide concentration that is greater than 6.5 wt % on liquor and a pH at 25° C. that is less than 1.3. The cellulose in the pretreated material is hydrolysed to glucose. The glucose may be fermented to a fermentation product such as ethanol.
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1 . A process for producing a fuel from softwood, said process comprising: (a) obtaining a feedstock comprising softwood; (b) pretreating the feedstock, said pretreating comprising heating the feedstock in a pretreatment liquor comprising sulfur dioxide and bisulfite salt, said heating conducted between 110° C. and 160° C., wherein the pretreatment liquor has a pH at 25° C. that is less than 1.3 and has a sulfur dioxide concentration that is greater than 6.5 wt % on liquor, (c) obtaining a slurry of pretreated material produced in (a), said slurry having a solid fraction comprising cellulose and a liquid fraction comprising solubilized hemicellulose; (d) hydrolyzing the cellulose to glucose, said hydrolyzing comprising adding cellulase to at least the solid fraction; (e) fermenting the glucose to a fermentation product, said fermenting comprising adding a microorganism to at least the glucose; and (f) recovering the fermentation product, wherein the fuel comprises the fermentation product. 2 . The process according to claim 1 , wherein the softwood comprises resinous softwood. 3 . The process according to claim 1 , wherein the softwood comprises pine, Douglas fir, or a combination thereof. 4 . The process according to claim 1 , wherein the feedstock comprises woodchips. 5 . The process according to claim 1 , wherein the feedstock comprises sawdust. 6 . The process according to claim 1 , wherein said heating is conducted between 120° C. and 150° C. 7 . The process according to claim 1 , wherein said heating is conducted for between 30 minutes and 4 hours. 8 . The process according to claim 1 , wherein the liquid to solid weight ratio in the pretreatment is between 1.5 and 9. 9 . The process according to claim 1 , wherein the concentration of sulfur dioxide in the pretreatment is between 7.8 wt % on liquor and 19.5 wt % on liquor. 10 . The process according to claim 1 , wherein the concentration of sulfur dioxide in the pretreatment is greater than 65 wt % on dry solids. 11 . The process according to claim 1 , wherein a concentration of alkali in the pretreatment is at least 0.05 wt % expressed as weight percent hydroxide on liquor. 12 . The process according to claim 1 , wherein a ratio of concentration of sulfur dioxide on liquor to concentration of alkali, expressed as weight percent hydroxide, on liquor is greater than 30. 13 . The process according to claim 1 , wherein a concentration of sulfur dioxide in the pretreatment is greater than 36 wt % on dry solids, and wherein a concentration of alkali is less than 0.25 wt % expressed as weight percent hydroxide on liquor. 14 . The process according to claim 1 , wherein the pH of the pretreatment liquor at 25° C. is between 0.9 and 1.1. 15 . The process according to claim 1 , wherein the pH of the slurry of pretreated material is less than 1. 16 . The process according to claim 1 , comprising: subjecting the slurry of pretreated material to a solid-liquid separation to separate the solid fraction and the liquid fraction; and washing the solid fraction produced by the solid-liquid separation with water, wherein adding cellulase to at least the solid fraction comprises adding the cellulase to the washed solid fraction. 17 . The process according to claim 1 , comprising producing one or more products from the liquid fraction, said one or more products comprising at least one of xylose, xylitol, methane, ethanol, or lignosulfonate. 18 . The process according to claim 1 , wherein the fermentation product is ethanol. 19 . A process for producing ethanol comprising: (a) obtaining a feedstock, said feedstock comprising softwood woodchips; (b) pretreating the feedstock, said pretreating comprising heating the feedstock in a pretreatment liquor comprising sulfur dioxide and bisulfite salt, said heating conducted between 110° C. and 160° C. for at least 30 minutes, wherein the pretreatment liquor has a pH at 25° C. that is less than 1.3 and has a sulfur dioxide concentration that is greater than 6.5 wt % on liquor; (c) obtaining a slurry of pretreated material produced in (a), said slurry having a solid fraction comprising cellulose and a liquid fraction comprising solubilized hemicellulose; (d) hydrolyzing the cellulose to glucose, said hydrolyzing comprising adding cellulase to at least the solid fraction; (e) fermenting the glucose to ethanol, said fermenting comprising adding a microorganism to at least the glucose; (f) recovering the ethanol; and (g) producing one or more products from the liquid fraction, said one or more products comprising at least one of xylose, xylitol, methane, ethanol, or lignosulfonate.
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Monosaccharides (2-ketogulonic acid C12P7/60) · CPC title
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Renewables or materials of biological origin · CPC title
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