US2014326421A1PendingUtilityA1
Processes for Purifying a Cellulosic Material
Est. expiryMay 3, 2033(~6.8 yrs left)· nominal 20-yr term from priority
Inventors:Denis G. FallonThomas S. GarrettLawton E. KizerBin LiRongfu LiJay MehtaTianshu PanXiaoyan TuLeslie AllenDinesh K. AroraPrabuddha BansalMichael T. Combs
D21C 3/20D21C 9/02D21C 11/0007D21C 9/005
46
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Claims
Abstract
A process for treating a cellulosic material comprising extracting the cellulosic material with an extractant to selectively extract hemicellulose therefrom and separating the extracted hemicellulose to form a cellulosic product comprising less hemicellulose than the cellulosic material. The extractant comprises a cellulose solvent and a co-solvent. The cellulosic product advantageously retains its cellulosic fiber morphology. The processes involve separating and recovering the hemicellulose and separating and recycling various process streams employed in the process.
Claims
exact text as granted — not AI-modifiedWe claim:
1 . A process for purifying a cellulosic material, comprising:
extracting hemicellulose from the cellulosic material with an extractant to form an intermediate cellulosic material having a reduced hemicellulose content; concentrating the intermediate cellulosic material to form a concentrated cellulosic material having an increased solids content; and recovering the separated hemicellulose; wherein the extractant comprises a cellulose solvent and a co-solvent, and the cellulose solvent is selected from the group consisting of an ionic liquid, an amine oxide and combinations thereof.
2 . The process of claim 1 , wherein the extracting forms an extraction mixture and wherein the extraction mixture is separated in a filter to form the intermediate cellulosic material and an extraction filtrate comprising the hemicellulose, the cellulose solvent and the co-solvent.
3 . The process of claim 2 , further comprising:
directing the extraction filtrate to a membrane to remove at least a portion of the cellulose solvent and the co-solvent from the extraction filtrate; and precipitating the extraction filtrate with a precipitation agent in a precipitator to form a precipitation slurry; wherein the precipitation agent is selected from the group consisting of alcohol, a ketone, a nitrile, an ether, an ester, a carboxylic acid, a halide, a hydrocarbon compound, an amine, a heterocyclic compound, water, and combinations thereof.
4 . The process of claim 3 , wherein the precipitation agent is selected from the group consisting of methanol, ethanol, isopropanol, butanol, acetone, 2-butanon, acetonitrile, propionitrile, butyronitrile, chloroacetonitrile, tetrahydrofuran, diethyl ether, dibutyl ether, methyl acetate, ethyl acetate, propyl acetate, isopropyl acetate, vinyl acetate, propylene carbonate, acetic acid, formic acid, formamide, dichloromethane, chloroform, 1-chlorobutane, 1,2-dichlorethane, hexane, 2,2,4-trimethylpentane, benzene, toluene, ethylamine, butylamine, ethyldiamine, pyridine, pyrrole, pyrrolidine, piperidine, water, and combinations thereof.
5 . The process of claim 2 , further comprising:
directing the extraction filtrate directly to a precipitator to precipitate the extraction filtrate with a precipitation agent to form a precipitation slurry.
6 . The process of claim 1 , wherein the extracting further comprises extracting impurities from the cellulosic material, wherein the impurities include degraded cellulose, resins, rosins, and/or other dichloromethane extractables.
7 . The process of claim 1 , wherein mono-, di-, and oligo-saccharide and other side products formed in the process are removed from the process.
8 . The process of claim 1 , wherein the concentrated cellulosic material is dried to recover a finished cellulosic product.
9 . The process of claim 1 , wherein the intermediate cellulosic material comprises at least 10 wt. % less hemicellulose than the cellulosic material.
10 . The process of claim 1 , wherein the extracting occurs from between 5 minutes and 180 minutes.
11 . The process of claim 1 , wherein the ionic liquid is selected from the group consisting of 1-butyl-3-methylimidazolium tetrachloroaluminate, 1-ethyl-3-methyl imidazolium tetrachloroaluminate, 1-ethyl-3-methyl imidalzolium hydrogensulfate, 1-butyl-3-methyl imidazolium hydrogensulfate, methylimidazolium chloride, 1-ethyl-3-methyl imidazolium acetate, 1,3-diethyl imidazolium acetate, 1-butyl-3-methyl imidazolium acetate, tris-2(hydroxyl ethyl)methylammonium methylsulfate, 1-ethyl-3-methyl imidazolium ethylsulfate, 1-ethyl-3-methyl imidazolium methanesulfonate, methyl-tri-n-butylammonium methylsulfate, 1-butyl-3-methyl imidazolium chloride, 1-ethyl-3-methyl imidasolium chloride, 1-ethyl-3-methyl imidazolium thiocyanate, 1-butyl-3-methyl imidazolium thiocyanate, 1-aryl-3-methyl imidazolium chloride, 1-ethyl-3-methylimidazolium dimethyl phosphate, 1-ethyl-3-methyl diethyl phosphate, 1,3-dimethylimidazolium dimethyl phosphate and combinations and complexes thereof.
12 . The process of claim 1 , wherein the co-solvent is selected from the group consisting of dimethyl sulfoxide, tetramethylene sulfone, tetramethylene sulfoxide, N,N-dimethylacetamide, N-methylpyrrolidone, dimethyl formamide, piperylene sulfone, acetic acid, water, and mixtures thereof.
13 . The process of claim 1 , wherein the amine oxide is selected from the group consisting of trimethylamine N-oxide, triethylamine N-oxide, tripropylamine N-oxide, tributylamine N-oxide, methyldiethylamine N-oxide, dimethylethylamine N-oxide, methyldipropylamine N-oxide, tribenzylamine N-Oxide, benzyldimethylamine N-oxide, benzyldiethylamine N-oxide, dibenzylmethylamine N-oxide, N-methylmorpholine N-oxide (NMMO), pyridine N-oxide, 2-, 3-, or 4-picoline N-oxide, N-methylpiperidine N-oxide, N-ethylpiperidine N-oxide N-propylpiperidine N-oxide, N-isopropylpiperidine N-oxide. N-butylpiperidine N-oxide, N-hexylpiperidine N-oxide. N-methylpyrrolidine N-oxide, N-ethylpyrrolidine N-oxide N-propylpyrrolidine N-oxide, N-isopropylpyrrolidine N-oxide. N-butylpyrrolidine N-oxide, N-hexylpyrrolidine N-oxide, and combinations thereof.
14 . The process of claim 1 , wherein the extracting hemicellulose comprises:
directing the cellulosic material and the extractant to an extractor; extracting hemicellulose from the cellulosic material in the extractor to form an extraction mixture; and filtering and washing the extraction mixture with an extractant wash to form the intermediate cellulosic material and an extraction filtrate.
15 . The process of claim 14 , wherein the extractant wash is selected from the group consisting of an alcohol, a ketone, a nitrile, an ether, an ester, a carboxylic acid, a halide, a hydrocarbon compound, an amine, a heterocyclic compound, water, and combinations thereof.
16 . The process of claim 14 , further comprising:
concentrating hemicellulose from the extraction filtrate in a hemicellulose concentrator to form a recovered extractant and a hemicellulose concentrate; and recycling the recovered extractant to the extractor or using it as an extractant wash.
17 . The process of claim 16 , further comprising:
precipitating the hemicellulose concentrate with a precipitation agent in a precipitator to form a precipitation slurry; filtering the precipitation slurry to form a precipitation agent filtrate and filtered hemicellulose; washing the filtered hemicellulose with a precipitant wash to form washed hemicellulose; and drying the washed hemicellulose to form a finished hemicellulose product.
18 . A process for purifying a cellulosic material, comprising:
extracting hemicellulose from the cellulosic material in an extractor with an extractant to form an intermediate cellulosic material having a reduced hemicellulose content; filtering and washing the intermediate cellulosic material to form a washed intermediate cellulosic material and an extraction filtrate; recovering recovered extractant from the extraction filtrate; and directing the recovered extractant to the extractor; wherein the extractant comprises a cellulose solvent and a co-solvent, and the cellulose solvent is selected from the group consisting of an ionic liquid, an amine oxide and combinations thereof.
19 . A process for purifying a cellulosic material, comprising:
extracting hemicellulose from the cellulosic material in an extractor with an extractant to form an intermediate cellulosic material having reduced hemicellulose content; filtering and washing the intermediate cellulosic material to recover an extraction filtrate comprising extractant and separated hemicellulose; precipitating the separated hemicellulose in a precipitator with a precipitation agent; and returning recovered extractant from the precipitator to the extractor; wherein the extractant comprises a cellulose solvent and a co-solvent, and the cellulose solvent is selected from the group consisting of an ionic liquid, an amine oxide and combinations thereof.
20 . The process of claim 19 , further comprising concentrating and drying the hemicellulose material to form a finished hemicellulose product comprising from 5 to 20 wt. % cellulose, from 70 to 95 wt. % hemicellulose, and from 3 to 20 wt. % water.Join the waitlist — get patent alerts
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