COMPOSITIONS COMPRISING C6 OLIGOSACCHARIDES |
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| 申请号 | EP12863319.5 | 申请日 | 2012-12-03 | 公开(公告)号 | EP2797944B1 | 公开(公告)日 | 2017-10-25 |
| 申请人 | Renmatix Inc.; | 发明人 | FLOYD, Daniel Clay; KADAM, Kiran L.; KILAMBI, Srinivas; | ||||
| 摘要 | Compositions comprising water-soluble C5 oligosaccharide hydrolysates are described, comprising C5 disaccharides, C5 trisaccharides, C5 tetrasaccharides, C5 pentasaccharides and C5 saccharides having a degree of polymerization of at least about 6. | ||||||
| 权利要求 | |||||||
| 说明书全文 | The present invention generally relates to compositions comprising C6 saccharides of varying degrees of polymerization, especially those processed from lignocellulosic biomass using supercritical, subcritical, and/or near critical fluid extraction. Among their many uses, the sugar streams may be converted to ethanol through fermentation using yeast or bacteria that feed on the sugars. As the sugars are consumed, ethanol and carbon dioxide are produced. The invention is directed to these compositions, as well as and other important ends. Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
In one embodiment, the invention is directed to compositions, comprising:
In further embodiments, the invention is directed to compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are compositions, comprising:
Described are methods of reducing the level of enzyme required for enzymatically hydrolyzing first water-soluble C6 saccharides having an average degree of polymerization to about 2 to about 15, preferably about 2 to about 10, and more preferably about 2 to about 6, to second water-soluble C6 saccharides having a lower average degree of polymerization than said average degree of polymerization of said first water-soluble C6 saccharides, comprising:
Described are methods of reducing the level of enzyme required for enzymatically hydrolyzing first water-soluble C5 saccharides having an average degree of polymerization to about 2 to about 28, preferably about 2 to about 15, more preferably about 2 to about 13, even more preferably about 2 to about 6, to second water-soluble C5 saccharides having a lower average degree of polymerization than said average degree of polymerization of said first water-soluble C5 saccharides, comprising:
The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention. In the drawings:
As employed above and throughout the disclosure, the following terms, unless otherwise indicated, shall be understood to have the following meanings. As used herein, the singular forms "a," "an," and "the" include the plural reference unless the context clearly indicates otherwise. While the present invention is capable of being embodied in various forms, the description below of several embodiments is made with the understanding that the present disclosure is to be considered as an exemplification of the invention, and is not intended to limit the invention to the specific embodiments illustrated. Headings are provided for convenience only and are not to be construed to limit the invention in any manner. Embodiments illustrated under any heading may be combined with embodiments illustrated under any other heading. The use of numerical values in the various quantitative values specified in this application, unless expressly indicated otherwise, are stated as approximations as though the minimum and maximum values within the stated ranges were both preceded by the word "about." In this manner, slight variations from a stated value can be used to achieve substantially the same results as the stated value. Also, the disclosure of ranges is intended as a continuous range including every value between the minimum and maximum values recited as well as any ranges that can be formed by such values. Also disclosed herein are any and all ratios (and ranges of any such ratios) that can be formed by dividing a recited numeric value into any other recited numeric value. Accordingly, the skilled person will appreciate that many such ratios, ranges, and ranges of ratios can be unambiguously derived from the numerical values presented herein and in all instances such ratios, ranges, and ranges of ratios represent various embodiments of the present invention. As used herein, the phrase "substantially free" means have no more than about 1%, preferably less than about 0.5%, more preferably, less than about 0.1 %, by weight of a component, based on the total weight of any composition containing the component. A supercritical fluid is a fluid at a temperature above its critical temperature and at a pressure above its critical pressure. A supercritical fluid exists at or above its "critical point," the point of highest temperature and pressure at which the liquid and vapor (gas) phases can exist in equilibrium with one another. Above critical pressure and critical temperature, the distinction between liquid and gas phases disappears. A supercritical fluid possesses approximately the penetration properties of a gas simultaneously with the solvent properties of a liquid. Accordingly, supercritical fluid extraction has the benefit of high penetrability and good solvation. Reported critical temperatures and pressures include: for pure water, a critical temperature of about 374.2°C, and a critical pressure of about 221 bar; for carbon dioxide, a critical temperature of about 31°C and a critical pressure of about 72.9 atmospheres (about 1072 psig). Near critical water has a temperature at or above about 300°C and below the critical temperature of water (374.2°C), and a pressure high enough to ensure that all fluid is in the liquid phase. Sub-critical water has a temperature of less than about 300°C and a pressure high enough to ensure that all fluid is in the liquid phase. Sub-critical water temperature may be greater than about 250°C and less than about 300°C, and in many instances sub-critical water has a temperature between about 250°C and about 280°C. The term "hot compressed water" is used interchangeably herein for water that is at or above its critical state, or defined herein as near-critical or sub-critical, or any other temperature above about 50°C (preferably, at least about 100°C) but less than subcritical and at pressures such that water is in a liquid state. As used herein, a fluid which is "supercritical" (e.g. supercritical water, supercritical CO2, etc.) indicates a fluid which would be supercritical if present in pure form under a given set of temperature and pressure conditions. For example, "supercritical water" indicates water present at a temperature of at least about 374.2°C and a pressure of at least about 221 bar, whether the water is pure water, or present as a mixture (e.g. water and ethanol, water and CO2, etc). Thus, for example, "a mixture of sub-critical water and supercritical carbon dioxide" indicates a mixture of water and carbon dioxide at a temperature and pressure above that of the critical point for carbon dioxide but below the critical point for water, regardless of whether the supercritical phase contains water and regardless of whether the water phase contains any carbon dioxide. For example, a mixture of sub-critical water and supercritical CO2 may have a temperature of about 250°C to about 280°C and a pressure of at least about 225 bar. As used herein, "lignocellulosic biomass or a component part thereof" refers to plant biomass containing cellulose, hemicellulose, and lignin from a variety of sources, including, without limitation (1) agricultural residues (including corn stover and sugarcane bagasse), (2) dedicated energy crops, (3) wood residues (including hardwoods, softwoods, sawmill and paper mill discards), and (4) municipal waste, and their constituent parts including without limitation, lignocellulose biomass itself, lignin, C6 saccharides (including cellulose, cellobiose, C6 oligosaccharides, C6 monosaccharides, C5 saccharides (including hemicellulose, C5 oligosaccharides, and C5 monosaccharides), and mixtures thereof. As used herein, "ash" refers to the non-aqueous residue that remains after a sample is burned, and consists mostly of metal oxides. Ash content may be measured in accordance with ASTM Standard Method No. E1755-01 "Standard Method for the Determination of Ash in Biomass." This test method covers the determination of ash, expressed as the percentage of residue remaining after dry oxidation at 550 to 600°C. All results are reported relative to the 105°C oven dry weight of the sample." See also: http://www.nrel.gov/biomass/pdfs/42622.pdf and http://www.astm.org/Standards/ E1755.htm, which are both incorporated herein by reference in their entirety. As used herein, "degree of polymerization" refers to the number of monomeric units in a macromolecule or polymer or oligomer molecule, including those monomeric units that are not identical (such as in a oligomer with different monomeric residues). The degree of polymerization (DP) of the various saccharides in the compositions of the invention may be measured using gel permeation chromatography (GPC), high pressure liquid chromatography (HPLC), such as DIONEX with an electrochemical detector, matrix-assisted laser desorption/ionization time-of-flight (MALDI-TOF) mass spectrometry, or other conventional molecular weight determination methods. Accordingly, in one embodiment, the invention is directed to compositions, comprising C6 saccharides. In particular compositions described, the compositions comprise:
Described are compositions, comprising:
In certain preferred embodiments, such compositions further comprise:
Described are compositions, comprising:
In certain preferred embodiments, such compositions further comprise:
Described are compositions, comprising:
In certain preferred embodiments, such compositions further comprise:
Described are compositions, comprising:
In certain preferred embodiments, such compositions further comprise:
Described are compositions, comprising:
In certain preferred embodiments, such compositions further comprise:
In certain compositions described, the water-soluble C6 oligosaccharide hydrolysate has a degree of polymerization of about 2 to about 15. In other embodiments, water-soluble C6 oligosaccharide hydrolysate has a degree of polymerization of about 2 to about 13. In other embodiments, water-soluble C6 oligosaccharide hydrolysate has a degree of polymerization of about 2 to about 10. In other embodiments, water-soluble C6 oligosaccharide hydrolysate has a degree of polymerization of about 2 to about 6. In certain embodiments, the compositions further comprise at least one water-soluble C6 monosaccharide hydrolysate. In certain embodiments, the water-soluble C6 monosaccharide hydrolysate is glucose, galactose, mannose, fructose, or a mixture thereof. In certain compositions described , the compositions further comprise less than about 10 ppm, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of aluminum, preferably less than about 5 ppm by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of aluminum. In certain compositions described , the compositions further comprise less than about 3000 ppm by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of calcium, preferably less than about 2950 ppm by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of calcium. In certain compositions described , the compositions further comprise less than about 350 ppm by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of iron, preferably less than about 325 ppm by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of iron. In certain compositions described , the compositions further comprise less than about 1000 ppm by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of sulfur, preferably less than about 975 ppm by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of sulfur. Described are compositions, wherein the ratio of the total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate to said elements is greater than about 45:1, preferably greater than about 47:1. In certain embodiments, the level of said elements are measured by inductively coupled plasma emission spectroscopy. In other compositions described , the compositions less than about 1500 mg of nitrogen per kg of total weight of water-soluble C6 saccharides, preferably less than about 1450 mg of nitrogen per kg of total weight of water-soluble C6 saccharides. Nitrogen may be measured by thermal conductivity detection after combustion and reduction. In other compositions described , the weight ratio of the collective mass of hydrogen and nitrogen to mass of carbon present in said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate is less than about 0.14. Carbon, hydrogen, and nitrogen levels may be measured by thermal conductivity detection after combustion and reduction. In certain other embodiments, the compositions comprising the C6 saccharides further comprise less than a maximum of any of the elements, individually or in combination, in the table listed below: In another embodiment, the compositions comprise:
In certain embodiments, said water-soluble C6 oligosaccharides are present at a level of 80% by weight to 92.5% by weight, based on total weight of C6 saccharides present in said composition. In certain embodiments of the composition, said water-soluble C6 oligosaccharides have a degree of polymerization of 2 to 13, preferably, 2 to 10, and more preferably 2 to 6. In certain embodiments, the compositions further comprise 5% by weight to 20% by weight, based on total weight of C6 saccharides present in said composition, of C6 monosaccharides. In certain compositions described herein, said water-soluble C6 oligosaccharide hydrolysate comprises:
In certain embodiments, the compositions further comprise:
In certain embodiments, the compositions further comprise:
In other embodiments, the compositions comprise:
wherein said C6 saccharides are extracted from lignocellulosic biomass. In other embodiments of the compositions, said C6 disaccharides are present at a level of 10% by weight to 20% by weight, based on total weight of C6 saccharides present in said composition. In other embodiments of the compositions, said C6 trisaccharides are present at a level of 10% by weight to 20% by weight, based on total weight of C6 saccharides present in said composition. In other embodiments of the compositions, said C6 tetrasaccharides are present at a level of 10% by weight to 20% by weight, based on total weight of C6 saccharides present in said composition. In other embodiments of the compositions, said C6 pentasaccharides are present at a level of 10% by weight to 20% by weight, based on total weight of C6 saccharides present in said composition. In other embodiments of the compositions, said C6 saccharides having at a degree of polymerization of at least 6 are present at a level of 10% by weight to 20% by weight, based on total weight of C6 saccharides present in said composition. Described are compositions, the compositions further comprise:
In certain embodiments, the compositions further comprise about 7.5% by weight to about 20% by weight, based on total weight of said water-soluble C6 oligosaccharide hydrolysate and said water-soluble C6 monosaccharide hydrolysate in said composition, of C6 monosaccharides. In other embodiments, the compositions further comprise water. In certain embodiments, C6 oligosaccharides are extracted from lignocellulosic biomass using supercritical, subcritical, or near critical water, or a combination thereof. Described are compositions, comprising C5 oligosaccharides. In particular, the compositions comprise:
Described arecompositions, comprising:
In certain embodiments, the elements are present at a level of less than about 3610 ppm in total by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition. Described arecompositions, comprising:
Described arecompositions, comprising:
Described arecompositions, comprising:
Described arecompositions, comprising:
Certain compositions described herein further comprise:
In certain compositions described, the water-soluble C5 oligosaccharide hydrolysate has a degree of polymerization of at least about 2 to about 28. In other embodiments, water-soluble C5 oligosaccharide hydrolysate has a degree of polymerization of at least about 2 to about 15. In other embodiments, water-soluble C5 oligosaccharide hydrolysate has a degree of polymerization of at least about 2 to about 10. In other embodiments, water-soluble C5 oligosaccharide hydrolysate has a degree of polymerization of at least about 2 to about 6. In certain compositions described, the compositions further comprise:
In certain compositions described, the water-soluble C5 monosaccharide hydrolysate is xylose, arabinose, lyxose, ribose, or a mixture thereof. In certain compositions described, the compositions further comprise less than about 10 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of aluminum, preferably less than about 5 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of aluminum. In certain compositions described, the compositions further comprise less than about 2300 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of calcium, preferably less than about 2250 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of calcium. In certain compositions described, the compositions further comprise less than about 50 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of iron, preferably less than about 30 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of iron. In certain compositions described, the compositions further comprise less than about 150 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of sulfur, preferably less than about 140 ppm by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of sulfur. In certain compositions described, the ratio of total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition to said elements is greater than about 75:1, preferably greater than about 80:1. In certain compositions described, the water-soluble C5 oligosaccharide hydrolysate is processed from lignocellulosic biomass using supercritical, subcritical, or near critical fluid extraction, or a combination thereof. In certain compositions described, the level of said elements are measured by inductively coupled plasma emission spectroscopy. In other compositions described, the compositions comprise less than about 350 ppm of nitrogen per kg of total weight of water-soluble C5 saccharides, preferably less than about 325 ppm of nitrogen per kg of total weight of water-soluble C6 saccharides. Nitrogen may be measured by thermal conductivity detection after combustion and reduction. In yet other compositionsdescribed , the weight ratio of the collective mass of hydrogen and nitrogen to mass of carbon present in said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate is less than about 0.14. Carbon, hydrogen, and nitrogen levels may be measured by thermal conductivity detection after combustion and reduction. In certain compositionsdescribed , the compositions comprising the C5 saccharides further comprise less than a maximum of any of the elements, individually or in combination, in the table listed below: In other compositions described, the compositions comprise:
In certain embodiments, said water-soluble C5 oligosaccharides are present at a level of 80% by weight to 90% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition. In certain embodiments of the composition, said water-soluble C5 oligosaccharides have a degree of polymerization of 2 to 16, preferably, 2 to 10, and more preferably, 2 to 5. In certain embodiments, the compositions further comprise 10% by weight, to 25% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of C5 monosaccharides. In certain compositionsdescribed herein, said water-soluble C5 oligosaccharide hydrolysate comprises:
In certain embodiments of the composition, said water-soluble C5 oligosaccharides have a degree of polymerization of 2 to 16, preferably, 2 to 10, and more preferably, 2 to 5. In certain embodiments, the compositions further comprise 10% by weight, to 25% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of C5 monosaccharides. In certain embodiments, the compositions further comprise 12.5% by weight, to 20% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of C5 monosaccharides. In certain compositions described herein, said C5 disaccharides are present at a level of 17.5% by weight to 25% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition. In certain compositions described herein, said C5 trisaccharides are present at a level of 12.5% by weight to 17.5% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition. In certain compositions described herein, said C5 tetrasaccharides are present at a level of 10% by weight to 20% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition. In certain compositions described herein, said C5 pentasaccharides are present at a level of 2.5% by weight to 15% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition. In certain compositions described herein, said C5 saccharides having at a degree of polymerization of at least 6 are present at a level of 12.5% by weight to 30% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition. In certain compositions described herein the compositions further comprise 10% by weight, to 25% by weight, based on total weight of said water-soluble C5 oligosaccharide hydrolysate and said water-soluble C5 monosaccharide hydrolysate in said composition, of C5 monosaccharides. In certain embodiments, the compositions described herein further comprise water. In certain described compositions, the water-soluble C6 oligosaccharide hydrolysate and the water-soluble C6 monosaccharide hydrolysate are processed from lignocellulosic biomass using supercritical, subcritical, or near critical fluid extraction, or a combination thereof. Described are methods of reducing the level of enzyme required for enzymatically hydrolyzing first water-soluble C6 saccharides having an average degree of polymerization to about 2 to about 15, preferably about 2 to about 10, and more preferably about 2 to about 6, to second water-soluble C6 saccharides having a lower average degree of polymerization than said average degree of polymerization of said first water-soluble C6 saccharides, comprising:
In certain embodiments, the C6 saccharides are extracted from lignocellulosic biomass. In other embodiments, the C6 saccharides are processed from lignocellulosic biomass using supercritical, subcritical, or near critical fluid extraction, or a combination thereof. Described are methods of reducing the level of enzyme required for enzymatically hydrolyzing first water-soluble C5 saccharides having an average degree of polymerization to about 2 to about 28, preferably about 2 to about 15, more preferably about 2 to about 13, even more preferably about 2 to about 6, to second water-soluble C5 saccharides having a lower average degree of polymerization than said average degree of polymerization of said first water-soluble C5 saccharides, comprising:
In further embodiments, the compositions further comprise less than 0.5% by weight, based on the total weight of said C5 saccharides or C6 saccharides, of organic solvent, such as alcohols, including water miscible lower aliphatic C1-C4 alcohols (e.g., methanol, ethanol, isopropanol, t-butanol). In preferred embodiments, the compositions contain less than 0.1% by weight, based on the total weight of said of said C5 saccharides or C6 saccharides of organic solvent. In more preferred embodiments, the compositions contain substantially no organic solvent. The compositions of the invention are preferably prepared from biomass by processes employing supercritical, subcritical, and/or near critical water, preferably without the addition of acid. The processes may include pretreatment step or steps using supercritical or near critical water to separate the C5 sugars (monomers and/or oligomers) from cellulose and lignin. In the pretreatment step, suitable temperatures are 130°C to 250°C, suitable pressures are 4 bars to 100 bars, and suitable residence times are 0.5 minutes to 5 hours. The processes may also include a cellulose hydrolysis step or steps using supercritical or near critical water to separate the cellulose (which may processed to form C6 monomeric and/or oligomeric sugars) from the lignin. In the hydrolysis step(s), suitable temperatures are 250°C to 450°C, suitable pressures are 40 bars to 260 bars, and suitable residence times are 0.1 seconds to 3 minutes. The compositions may be prepared in any suitable reactor, including, but not limited to, a tubular reactor, a digester (vertical, horizontal, or inclined), or the like. Suitable digesters include the digester system described in US-B-8,057,639, which include a digester and a steam explosion unit. The compositions of the invention comprising C5 saccharides or C6 saccharides may be utilized in a wide variety of applications, where C5 and C6 sugars are conventionally utilized, including, but not limited to, the production of various chemicals and fuels using fermentative, enzymatic, catalytic, and non-catalytic (e.g., thermal decomposition) processes. Such processes are useful for preparing feedstocks for the preparation of the following non-exhaustive list:
The present invention is further defined in the following Examples, in which all parts and percentages are by weight, unless otherwise stated. It should be understood that these examples, while indicating preferred embodiments of the invention, are given by way of illustration only and are not to be construed as limiting in any manner. From the above discussion and these examples, one skilled in the art can ascertain the essential characteristics of this invention, and without departing from the spirit and scope thereof, can make various changes and modifications of the invention to adapt it to various usages and conditions. The C5 oligosaccharide compositions and the C6 oligosaccharide compositions of the invention were prepared using supercritical, subcritical, and near critical water extraction in a two stage process. Particulate lignocellulosic biomass consisting of mixed hardwood chips of 140 mesh or less was mixed with water to form a slurry (about 20% by weight solids). The slurry was heated to a temperature of 170-245°C and then feed into a pretreatment reactor for 1-120 minutes under sufficient pressure to keep the water in the liquid phase. The pretreated slurry was then cooled to a temperature less than about 100°C under little (less than about 10 bar) or no pressure. The pretreated solids were then separated from the liquid stream using a filter press. Alternatively, the solids may be separated using a centrifugal filter pressor. The pretreated solids were then mixed with water to form a slurry and the slurry was heated to a temperature of 150-250°C. The slurry was then subjected to supercritical water at 374-600°C in a hydrolysis reactor for 0.05-10 seconds under a pressure of 230-300 bar. After exiting the hydrolysis reactor, the hydrolyzed slurry was quenched with water and then flashed to about ambient temperature and pressure to remove water. The lignin solids were then separated from the liquid stream using a centrifugal decanter and air dried. The C5 oligosaccharides and the C6 oligosaccharides streams were first concentrated to about 200 g/L, adjusted to about pH 3-4 and filtered using 0.45 micron filter. The dried compositions containing the C5 and C6 oligosaccharides of Example 1 were analyzed using inductively coupled plasma emission spectroscopy. The results are shown in the table below: The C5 oligosaccharide compositions and the C6 oligosaccharide compositions of the invention were prepared using supercritical, subcritical, and near critical water extraction in a two stage process as described in Example 1. The samples were then diluted ten times. The degree of polymerization was qualitatively determined, i.e., not quantifying the amount of each oligomer, using gel permeation chromatography. As can be seen in The C6 saccharide compositions of the invention were prepared using supercritical, subcritical, and near critical water extraction in a two stage process as described in Example 1. Representative samples bracketing the extremes/possibilities of feed material source (tubular reactor), reactor temperature (348.2-383.4°C), reactor residence time (0.19-1.48 seconds), and feed aqueous slurry concentration (6.4-14.77%) were selected. The representative samples were analyzed using gel permeation chromatography. The area under each peak (indicating an individual mer unit in the saccharide) was measured to calculate weight % of each mer unit, based on the total weight of C6 saccharides present in the sample. The results are shown in the following table: The C5 saccharide compositions were prepared using supercritical, subcritical, and near critical water extraction in the first stage of the two stage process as described in Example 1. Representative samples bracketing the extremes/possibilities of reactor feed concentration (10.66-13.78 weight %, reactor temperature (249-261 °C), and reactor residence time (2-3 minutes) were selected. The representative samples were analyzed using gel permeation chromatography (details below). The area under each peak (indicating an individual mer unit in the saccharide) was measured to calculate weight % of each mer unit, based on the total weight of C5 saccharides present in the sample. The results are shown in the following table: The C5 compositions and the C6 saccharide compositions of the invention were prepared using supercritical, subcritical, and near critical water extraction in the two stage process as described in Example 1. Representative samples were selected. The representative samples were analyzed using DIONEX HPLC (details below). The results are averaged and shown in the tables below: When ranges are used herein for physical properties, such as molecular weight, or chemical properties, such as chemical formulae, all combinations, and subcombinations of ranges specific embodiments therein are intended to be included. The disclosures of each patent, patent application, and publication cited or described in this document are hereby incorporated herein by reference, in their entirety. Those skilled in the art will appreciate that numerous changes and modifications can be made to the preferred embodiments of the invention and that such changes and modifications can be made without departing from the spirit of the invention. It is, therefore, intended that the appended claims cover all such equivalent variations as fall within the true spirit and scope of the invention. |
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