Sugar Separation and Purification Through Filtration
Methods are disclosed that separate xylose from glucose in pretreated and enzyme-hydrolyzed cellulosic and/or lignocellulosic biomass. Filtration, especially diafiltration is used to reduce fermentation-impeding substances and xylose from glucose and growth-promoting factors.
1 .- 312 . (canceled)
313 . A method of clarifying and refining a sugar hydrolyzate comprising C5 sugars and C6 sugars, the method comprising: contacting the sugar hydrolyzate with a first nanofiltration membrane to produce a C6 enriched retentate and a C5 enriched filtrate, wherein the contacting is diafiltration and wherein water is added to the sugar hydrolyzate during the contacting.
314 . The method of claim 313 , further comprising contacting the sugar hydrolyzate with an ultrafiltration membrane to remove color molecules and suspended solids.
315 . The method of claim 314 , wherein the sugar hydrolyzate is contacted with the ultrafiltration membrane prior to the first nanofiltration membrane.
316 . The method of claim 313 , further comprising contacting the sugar hydrolyzate with a second nanofiltration membrane to remove one or more inhibitors.
317 . The method of claim 316 , wherein the one or more inhibitors are removed prior to producing the C6 enriched retentate and the C5 enriched retentate.
318 . The method of claim 313 , further comprising contacting the C6 enriched retentate or the C5 enriched retentate with a reverse osmosis membrane to concentrate the C6 or C5 sugars.
319 . The method of claim 316 , wherein the one or more inhibitors comprise furfural, hydroxymethylfurfural, acetic acid, formic acid, or a combination thereof.
320 . The method of claim 313 , wherein the first nanofiltration membrane is a spiral wound nanofiltration membrane.
321 . The method of claim 313 , wherein contacting the sugar hydrolyzate with the first nanofiltration membrane or the second nanofiltration membrane is performed at a pressure of about 250 psi to about 750 psi.
322 . The method of claim 313 , wherein the water is added when a retentate volume reaches from about 10% to about 75% of a starting volume of the sugar hydrolyzate.
323 . The method of claim 313 , wherein the C6 sugars comprise glucose.
324 . The method of claim 313 , wherein the C5 sugars comprise xylose, arabinose, or a combination thereof.
325 . The method of claim 313 , wherein the sugar hydrolyzate was produced by pretreating or hydrolyzing a biomass comprising cellulosic, hemicellulosic, or lignocellulosic material.
326 . A method of refining a sugar hydrolyzate comprising C5 sugars and C6 sugars, the method comprising:
(a) contacting the sugar hydrolyzate with a microfiltration or ultrafiltration membrane to remove color molecules and suspended solids;
(b) contacting the sugar hydrolyzate with a first nanofiltration membrane to remove one or more inhibitors; and
(c) contacting the sugar hydrolyzate with a second nanofiltration membrane to produce a C6 enriched retentate and a C5 enriched filtrate.
327 . A system for refining a sugar hydrolyzate, the system comprising:
(a) a sugar hydrolyzate comprising C5 sugars and C6 sugars produced by pretreating or hydrolyzing of a biomass comprising cellulosic, hemicellulosic, or lignocellulosic material;
(b) a first nanofiltration membrane that produces a C6 enriched retentate and a C5 enriched filtrate when the sugar hydrolyzate is contacted with the first nanofiltration membrane; and
(c) a water source that adds water to the sugar hydrolyzate when the sugar hydrolyzate is contacted with the first nanofiltration membrane.
328 . The system of claim 327 , further comprising an ultrafiltration membrane to remove color molecules and suspended solids from the sugar hydrolyzate.
329 . The system of claim 328 , wherein the sugar hydrolyzate is contacted with the ultrafiltration membrane prior to the first nanofiltration membrane.
330 . The system of claim 327 , further comprising a second nanofiltration membrane to remove one or more inhibitors from the sugar hydrolyzate.
331 . The system of claim 330 , wherein the sugar hydrolyzate is contacted with the second nanofiltration membrane prior to the first nanofiltration membrane.
332 . The system of claim 327 , further comprising a reverse osmosis membrane to concentrate the C6 or the C5 sugars in the C6 enriched retentate or the C5 enriched filtrate.