Abstract:
In some variations, this invention provides a process for producing fermentable sugars from cellulosic biomass, comprising: extracting biomass with steam or hot water to produce an extract liquor containing hemicellulose oligomers, dissolved lignin, and cellulose-rich solids; separating and washing the cellulose-rich solids; removing a portion of glucan contained in the washed cellulose-rich solids as glucose oligomers using a liquefaction-focused blend of enzymes; co-hydrolyzing glucose oligomers and hemicellulose oligomers, with enzymes or chemical catalyst, to produce glucose and hemicellulose monomers; and recovering the glucose and hemicellulose monomers as fermentable sugars. The liquefaction-focused blend of enzymes contains endoglucanases and exoglucanases. Optionally, the glucose and the hemicellulose monomers may be recovered as separate streams. The residual cellulose (not hydrolyzed) as well as the lignin may be recovered and combusted, or utilized for other purposes, such as for energy-dense pellets.
Abstract:
Conventionally, sugarcane processing avoids leaving residual sucrose in the bagasse, since the bagasse will be burned and the value of the sucrose would be lost. However, when coupled with a Green Power+® process to extract hemicelluloses, sucrose may also be extracted and recovered from the bagasse. In some variations, a process includes mechanically treating a feedstock to generate a sucrose-rich stream and lignocellulosic material that intentionally retains a significant amount of the initial sucrose in the feedstock; extracting the lignocellulosic material with steam and/or hot water to produce cellulose-rich solids and an extract liquor containing hemicellulosic oligomers and sucrose; and then hydrolyzing the hemicellulosic oligomers into a hemicellulose sugar stream. Each of the sucrose-rich stream and the hemicellulose sugar stream (containing the starting residual sucrose) may be recovered or further processed (e.g., fermented to ethanol). Similar processes are possible with energy cane, sugar beets, and energy beets.
Abstract translation:通常,甘蔗加工避免了将蔗糖残留在甘蔗渣中,因为甘蔗渣将被燃烧并且蔗糖的值将丢失。 然而,当与Green Power +工艺一起提取半纤维素时,蔗糖也可以从蔗渣中提取和回收。 在一些变型中,方法包括机械处理原料以产生富含蔗糖的料流和有意地在原料中保留大量初始蔗糖的木质纤维素材料; 用蒸汽和/或热水提取木质纤维素材料以产生富含纤维素的固体和含有半纤维素低聚物和蔗糖的提取液; 然后将半纤维素低聚物水解成半纤维素糖流。 可以回收或进一步处理每种富含蔗糖的料流和半纤维素糖料流(含有起始残留的蔗糖)(例如发酵成乙醇)。 类似的过程可能与能量甘蔗,甜菜和能量甜菜。
Abstract:
This disclosure provides a business method and system for generating sugars and recycling a non-biomass component from a waste stream. In some embodiments, a waste stream comprising cellulose and a non-biomass component is saccharified to produce glucose, followed by recovery of the glucose and non-biomass component, which may be recycled to another site associated with production of a cellulose-containing product that contains the non-biomass component. In certain scenarios, the waste stream is generated at a first location, cellulose pretreatment (if desired) and hydrolysis are conducted at a second location, and the non-biomass component is recycled to the first location or a third location. The non-biomass component may include metals, metal oxides, salts, organic compounds, inorganic compounds, oligomers, or polymers, for example.
Abstract:
In some variations, the invention provides a process for producing furfural, 5-hydroxymethylfurfural, and/or levulinic acid from cellulosic biomass, comprising: fractionating the feedstock in the presence of a solvent for lignin, sulfur dioxide, and water, to produce a liquor containing hemicellulose, cellulose-rich solids, and lignin; hydrolyzing the hemicellulose contained in the liquor, to produce hemicellulosic monomers; dehydrating the hemicellulose to convert at least a portion of C5 hemicelluloses to furfural and to convert at least a portion of C6 hemicelluloses to 5-hydroxymethylfurfural; converting at least some of the 5-hydroxymethylfurfural to levulinic acid and formic acid; and recovering at least one of the furfural, the 5-hydroxymethylfurfural, or the levulinic acid. Other embodiments provide a process for dehydrating hemicellulose to convert oligomeric C5 hemicelluloses to furfural and to convert oligomeric C6 hemicelluloses to 5-hydroxymethylfurfural. The furfural may be converted to succinic acid, or to levulinic acid, for example.
Abstract:
In some variations, the invention provides a process for producing purified cellulose, comprising: providing a feedstock comprising lignocellulosic biomass; contacting the feedstock with sulfur dioxide, water, and a solvent for lignin, to produce intermediate solids and a liquid phase comprising hemicelluloses and lignin; mildly bleaching the intermediate solids to further delignify the intermediate solids, thereby generating cellulose-rich solids; and washing the cellulose-rich solids to generate purified cellulose with less than 2 weight percent lignin. The bleaching may employ bleaching agents including lignin-modifying enzymes. The bleaching and washing steps may be combined. It is also possible to carry out bleaching prior to, or simultaneously with, biomass fractionation in the digestor, which may help reduce downstream lignin precipitation. The purified cellulose may be utilized for making cellulose materials or cellulose derivatives, or for hydrolysis to produce glucose.
Abstract:
This invention provides processes and apparatus to convert biomass, including wood and agricultural residues, into low-ash biomass pellets for combustion, alone or in combination with another solid fuel. Some embodiments provide processes for producing low-ash biomass from cellulosic biomass, comprising providing an aqueous extraction solution with acetic acid; extracting the feedstock to produce an extract liquor containing soluble ash, hemicellulosic oligomers, acetic acid, dissolved lignin, and cellulose-rich solids; dewatering and drying the cellulose-rich, lignin-rich solids to produce a low-ash biomass; hydrolyzing the hemicellulosic oligomers to produce hemicellulosic sugars, wherein additional acetic acid is generated; removing a vapor stream comprising vaporized acetic acid from the extract; and recycling the vapor or its condensate to provide some starting acetic acid for the extraction solution. The disclosed processes can produce clean power from biomass. Co-products may include fermentable sugars, fermentation products such as ethanol, fertilizers, and lignin.
Abstract:
This invention provides processes to convert biomass into energy-dense biomass for combustion, alone or in combination with another solid fuel. In some variations, biomass is extracted to produce an extract liquor containing hemicellulosic oligomers and cellulose-rich solids; hemicellulosic oligomers are removed; and the cellulose-rich solids are torrefied to produce energy-dense biomass. In some embodiments, hydrotorrefaction is employed to produce hydrophobic, energy-dense biomass in an energy-efficient process that avoids intermediate drying between extraction/hydrolysis and torrefaction. The energy-dense biomass may be pelletized or directly combusted or gasified. The hemicellulosic oligomers may be hydrolyzed to fermentable sugars and then fermented to ethanol or other products, or further reacted to produce furfural or other products.
Abstract:
What is disclosed is a biorefining process to co-produce xylitol with ethanol or other products. In some variations, a process for producing ethanol and xylitol from lignocellulosic biomass, comprises: extracting hemicelluloses from lignocellulosic biomass, wherein the hemicelluloses include xylose oligomers and other sugar oligomers; hydrolyzing the xylose oligomers and the other sugar oligomers, using an acid catalyst or enzymes, to generate xylose and other sugar monomers, respectively; fermenting the other sugar monomers to ethanol using a suitable ethanol-producing microorganism; removing at least some of the ethanol (to increase concentration of xylose); fermenting the xylose to xylitol using a suitable xylitol-producing microorganism; and recovering the xylitol at high concentration.
Abstract:
Processes disclosed are capable of converting biomass into high-crystallinity nanocellulose with low mechanical energy input. In some variations, the process includes fractionating biomass with sulfur dioxide or a sulfite compound and water, to generate cellulose-rich solids and a liquid containing hemicellulose and lignin; and mechanically treating the cellulose-rich solids to form nanofibrils and/or nanocrystals. The total mechanical energy may be less than 500 kilowatt-hours per ton. The crystallinity of the nanocellulose material may be 80% or higher, translating into good reinforcing properties for composites. The nanocellulose material may include nanofibrillated cellulose, nanocrystalline cellulose, or both. In some embodiments, the nanocellulose material is hydrophobic via deposition of some lignin onto the cellulose surface. Optionally, sugars derived from amorphous cellulose and hemicellulose may be separately fermented, such as to monomers for various polymers. These polymers may be combined with the nanocellulose to form completely renewable composites.
Abstract:
Some variations provide a new nanolignocellulose composition comprising, on a bone-dry, ash-free, and acetyl-free basis, from 35 wt % to 80 wt % cellulose nanofibrils, cellulose microfibrils, or a combination thereof, from 15 wt % to 45 wt % lignin, and from 5 wt % to 20 wt % hemicelluloses. The hemicelluloses may contain xylan or mannan as the major component. Novel properties arise from the hemicellulose content that is intermediate between high hemicellulose content of raw biomass and low hemicellulose content of conventional nanocellulose. The nanolignocellulose composition is hydrophobic due to the presence of lignin. Processes for making and using the nanolignocellulose compositions are also described.