专利摘要:
Compositions comprising lignin and low levels of undesirable impurities, such as compounds containing sulfur, nitrogen, or metals, are disclosed.
公开号:AU2012362936A1
申请号:U2012362936
申请日:2012-12-03
公开日:2014-07-03
发明作者:Kiran L. Kadam;Srinivas Kilambi
申请人:Renmatix Inc;
IPC主号:C08L97-00
专利说明:
WO 2013/101397 PCT/US2012/067535 COMPOSITIONS COMPRISING LIGNIN CROSS REFERENCE TO RELATED APPLICATIONS [0001] This application claims the benefit of U.S. Application No. 61/581,865, filed December 30, 2011, and U.S. Application No. 13/472,798 filed May 16, 2012, the entire disclosures of which are incorporated herein by reference. FIELD OF THE INVENTION [0002] The present invention generally relates to compositions comprising lignin containing maximum levels of undesirable impurities, such as compounds containing sulfur, nitrogen, or metals. BACKGROUND OF THE INVENTION [0003] There are a number of processes for converting lignocellulosic biomass into liquid streams of various sugars. Certain preferred processes are based on supercritical water (SCW) or hot compressed water (HCW) technology, which offer several advantages including high throughputs, use of mixed feedstocks, separation of sugars, and avoidance of concentrated acids, microbial cultures, and enzymes. Processes using hot compressed water may have two distinct operations: pre treatment and cellulose hydrolysis. The pre-treatment process hydrolyzes the hemicellulose component of the lignocellulosic biomass and cellulose hydrolysis (CH) process hydrolyzes the cellulose fibers. The resultant five carbon (C5) and six carbon (C6) sugar streams are recovered separately. The remaining solids, which consist mostly of lignin, are preferably recovered, such as through filtration, and may be used as a fuel to provide thermal energy to the process itself or for other processes. Lignin has the combustion heat of 26.6 KJ/g, and holds highest energy among all natural polymeric compounds that contain carbon, hydrogen and oxygen. In energy, lignin is equivalent to ethanol, which also contains carbon, hydrogen and oxygen, and has the combustion heat of 30 KJ/g. However, for a given volume, lignin's combustion heat is approximately 1.5 times as much as that of ethanol, because of lignin's higher density. 1 WO 2013/101397 PCT/US2012/067535 http://www.altenergymag.com/emagazine/2009/06/lig n in-as-alternative-renewable fuel/1384). Thus, lignin serves as a useful renewable energy source. [0004] Lignocellulosic biomass contains cellulose, hemicellulose, and lignin, along with minor amounts of proteins, lipids (fats, waxes, and oils) and minerals. About two thirds of the dry mass of cellulosic materials is present as cellulose and hemicellulose with lignin making up the bulk of the remaining dry mass. Lignin is a cross-linked racemic macromolecule with a molecular masse in excess of 10,000 Daltons. It is relatively hydrophobic and aromatic in nature. The degree of polymerization in nature is difficult to measure, since it is fragmented during extraction and the molecule consists of various types of substructures that appear to repeat in a haphazard manner. Different types of lignin have been described depending on the means of isolation. "Lignin and its Properties: Glossary of Lignin Nomenclature," Dialogue/Newsletters Volume 9, Number 1, Lignin Institute, July 2001. [0005] There are three monolignol monomers, methoxylated to various degrees: p coumaryl alcohol, coniferyl alcohol, and sinapyl alcohol. K. Freudenberg & A.C. Nash (eds) (1968). Constitution and Biosynthesis of Lignin. Berlin: Springer-Verlag. These lignols are incorporated into lignin in the form of the phenylpropanoids p-hydroxyphenyl (H), guaiacyl (G), and syringal (S), respectively. W. Boerjan, J. Ralph, M. Baucher (June 2003). "Lignin bios". Ann. Rev. Plant Biol. 54 (1): 519-549. Gymnosperms have a lignin that consists almost entirely of G with small quantities of H. That of dicotyledonous angiosperms is more often than not a mixture of G and S (with very little H), and monocotyledonous lignin is a mixture of all three. Id. Many grasses have mostly G, while some palms have mainly S. All lignins contain small amounts of incomplete or modified monolignols, and other monomers are prominent in non-woody plants. J. Ralph, et al. (2001). "Elucidation of new structures in lignins of CAD- and COMT-deficient plants by NMR." Phytochem. 57 (6): 993-1003. [0006] Impurities may be introduced into lignin via processing of the lignocellulosic biomass. Since lignin compositions may be used as a fuel in the SCW or HCW process or other processes, they preferably have a low level of contaminants or impurities that contribute to health, environmental, and safety concerns. For example, it is highly desirable to have no or only a low level of compounds containing sulfur in the lignin 2 WO 2013/101397 PCT/US2012/067535 composition, as the presence of sulfur may contribute to SOx emissions, when the lignin is combusted. In other applications, low levels of sulfur may also be desirable if lignin is chemically converted through a catalytic process to a downstream product or a derivative. Low levels of sulfur within the final product may also be desirable from product acceptance criteria, or low levels of sulfur may help prevent premature catalyst deactivation for such chemical conversions. [0007] Accordingly, the invention is directed to lignin compositions having low levels of impurities, as well as other important ends. SUMMARY OF THE INVENTION [0008] In one embodiment, the invention is directed to compositions, comprising: lignin; and less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn. In some embodiments, the compositions further comprise less than about 700 mg of calcium per kg of said lignin. In other embodiments, the compositions further comprise less than about 525 mg of iron per kg of said lignin. In yet other embodiments, the compositions further comprise less than about 150 mg of sulfur per kg of said lignin. In some embodiments, the compositions further comprise less than about 20 g of ash per kg of said lignin. In other embodiments, the compositions comprise less than about 2000 mg of nitrogen per kg of said lignin. In yet other embodiments, the compositions further comprise a weight ratio of the total mass of hydrogen and nitrogen to carbon of less than about 0.110. [0009] In other embodiments, the invention is directed to compositions, comprising: lignin; less than about 700 mg of calcium per kg of said lignin; less than about 525 mg of iron per kg of said lignin; and less than about 150 mg of sulfur per kg of said lignin. 3 WO 2013/101397 PCT/US2012/067535 In some embodiments, the compositions comprise less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn. [0010] In yet other embodiments, the invention is directed to compositions, comprising: lignin; and less than about 700 mg of calcium per kg of said lignin. In some embodiments, the compositions comprise less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn. [0011] In yet further embodiments, the invention is directed to compositions, comprising: lignin; and less than about 525 mg of iron per kg of said lignin. In some embodiments, the compositions comprise less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn. [0012] In yet another embodiment, the invention is directed to compositions, comprising: lignin; and less than about 150 mg of sulfur per kg of said lignin. In some embodiments, the compositions comprise less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn. DETAILED DESCRIPTION OF THE INVENTION [0013] As employed above and throughout the disclosure, the following terms, unless otherwise indicated, shall be understood to have the following meanings. 4 WO 2013/101397 PCT/US2012/067535 [0014] As used herein, the singular forms "a," "an," and "the" include the plural reference unless the context clearly indicates otherwise. [0015] 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. [0016] 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. [00171 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. [0018] 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 5 WO 2013/101397 PCT/US2012/067535 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. [0019] Reported critical temperatures and pressures include: for pure water, a critical temperature of about 374.20C, and a critical pressure of about 221 bar; for carbon dioxide, a critical temperature of about 31 0 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 (374.20C), 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 3000C and a pressure high enough to ensure that all fluid is in the liquid phase. Sub-critical water temperature may be greater than about 2500C and less than about 3000C, and in many instances sub-critical water has a temperature between about 2500C and about 2800C. 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 500C (preferably, at least about 1000C) but less than subcritical and at pressures such that water is in a liquid state. [0020] As used herein, a fluid which is "supercritical" (e.g. supercritical water, supercritical C02, 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 374.20C 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 C02, 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 C02 may have a temperature of about 2500C to about 2800C and a pressure of at least about 225 bar. 6 WO 2013/101397 PCT/US2012/067535 [0021] 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, C 5 saccharides (including hemicellulose, C5 oligosaccharides, and C5 monosaccharides), and mixtures thereof. [0022] 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 6000C. All results are reported relative to the 105'C oven dry weight of the sample." See also: http://www.nrel.qov/biomass/pdfs/42622.pdf and http://www.astm.orq/Standards/ El 755.htm, which are both incorporated herein by reference in their entirety. [00231 Accordingly, in one embodiment, the invention is directed to compositions, comprising: lignin; and less than about 2000 mg, preferably less than about 1775 mg, in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn. [0024] In other embodiments, the invention is directed to compositions, comprising: lignin; less than about 700 mg, preferably less than about 675 mg, of calcium per kg of said lignin; less than about 525 mg, preferably less than about 505 mg, of iron per kg of said lignin; and 7 WO 2013/101397 PCT/US2012/067535 less than about 150 mg, preferably less than about 147 mg, of sulfur per kg of said lignin. [0025] In some embodiments, the compositions comprise: lignin; and less than about 700 mg, preferably less than about 675 mg, of calcium per kg of said lignin. [0026] In some embodiments, the compositions comprise: lignin; and less than about 525 mg, preferably less than about 505 mg, of iron per kg of said lignin. [0027] In some embodiments, the compositions comprise: lignin; and less than about 150 mg, preferably less than about 147 mg, of sulfur per kg of said lignin. [0028] In some embodiments, the compositions comprise less than about 2000 mg, preferably less than 1775 mg, in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn. [0029] In some embodiments, the compositions further comprise less than about 700 mg, preferably less than about 675 mg, of calcium per kg of said lignin. In other embodiments, the compositions further comprise less than about 525 mg of iron per kg of said lignin. In yet other embodiments, the compositions further comprise less than about 150 mg of sulfur per kg of said lignin. [0030] In some embodiments, the lignin has a heating value as measured by ASTM D240 and D5865 of at least about 5,000 BTU/lb, preferably at least about 7,500 BTU/lb, and more preferably, at least about 8,000 BTU/lb. 8 WO 2013/101397 PCT/US2012/067535 [0031] In some embodiments, the lignin has an average particle size less than about 500 microns. In preferred embodiments, the lignin has an average unaggregated particle size less than about 100 microns. In other preferred embodiments, the lignin has an average unaggregated particle size less than about 60 microns. [0032] In some embodiments, the lignin has a bulk density of less than about 0.35 g/cc, depending upon particle size. [0033] In some embodiments, the lignin is processed from lignocellulosic biomass optionally using supercritical, subcritical, or near critical fluid extraction or combinations thereof. [0034] In some embodiments, the composition is substantially free of organic solvent. [0035] In some embodiments, the lignin is in a powdered form. In other embodiments, the lignin is in a pelletized form. In yet other embodiments, the lignin is in a liquid form. In addition, the lignin may be in combination of these forms. [0036] In some embodiments, is present at a level of at least 30% by weight, based on the total weight of the composition, as measured by pyrolysis molecular beam mass spectrometry. [00371 In some embodiments, the weight ratio of syringyl monolignol to guaiacyl monolignol is about 2.0 to about 3.0, as measured by pyrolysis molecular beam mass spectrometry. [0038] In some embodiments, the compositions further comprise less than about 700 mg, preferably less than about 675 mg, of calcium per kg of said lignin. [0039] In some embodiments, the compositions further comprise less than about 525 mg, preferably less than about 505 mg, of iron per kg of said lignin. [0040] In some embodiments, the compositions further comprise less than about 150 mg, preferably less than about 147 mg, of sulfur per kg of said lignin. 9 WO 2013/101397 PCT/US2012/067535 [0041] In some embodiments, the levels of said elements are measured by inductively coupled plasma emission spectroscopy. [0042] In some embodiments, the compositions further comprise less than about 20 g of ash per kg of said lignin, preferably less than about 17.5 g of ash per kg of said lignin. [0043] In other embodiments, the compositions comprise less than about 2000 mg of nitrogen per kg of said lignin, preferably less than about 1900 mg of nitrogen per kg of said lignin. Nitrogen may be measured by thermal conductivity detection after combustion and reduction. [0044] In yet other embodiments, the compositions further comprise a weight ratio of the total mass of hydrogen and nitrogen to carbon of less than about 0.110, preferably less than about 0.105. Carbon, hydrogen, and nitrogen levels may be measured by thermal conductivity detection after combustion and reduction. [0045] In certain other embodiments, the compositions comprising the lignin further comprise less than a maximum of any of the elements, individually or in combination, in the table listed below: Element Level less than about (mg of element/kg of lignin) Al 50 As 16 B 3.25 Ba 3.7 Be 0.04 Cd 0.850 Co 1.25 Cr 2.0 Cu 20.0 K 45.0 Li 0.310 Mg 22.5 Mn 7.00 Mo 3.00 10 WO 2013/101397 PCT/US2012/067535 Element Level less than about (mg of element/kg of lignin) Na 61.5 Ni 1.50 P 115 Pb 10.00 Sb 9.50 Se 21.0 Si 65.0 Sn 11.00 Sr 2.25 Ti 6.00 TI 21.0 V 0.350 Zn 11.5 [0046] In further embodiments, the compositions further comprise less than about 0.5% by weight, based on the total weight of said lignin, of organic solvent, such as alcohols, including water miscible lower aliphatic C1C4 alcohols (e.g., methanol, ethanol, isopropanol, t-butanol). In preferred embodiments, the compositions contain less than about 0.1% by weight, based on the total weight of said lignin of organic solvent. In more preferred embodiments, the compositions contain substantially no organic solvent. [0047] 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 about 130'C to about 250*C, suitable pressures are about 4 bars to about 100 bars, and suitable residence times are about 0.5 minutes to about 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 about 2500C to about 450 0 C, suitable pressures are about 40 bars to about 260 bars, and suitable residence times are about 0.1 seconds to about 3 minutes. 11 WO 2013/101397 PCT/US2012/067535 [0048] The compositions of the invention 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 entire disclosure of which is incorporated by reference. [0049] The compositions of the invention comprising lignin may be utilized in a variety of applications, including, but not limited to, fuels, tackifiers, phenol formaldehyde resin extenders in the manufacture of particle board and plywood, in the manufacture of molding compounds, urethane and epoxy resins, antioxidants, controlled-release agents, flow control agents, cement/concrete mixing, plasterboard production, oil drilling, general dispersion, tanning leather, road covering, vanillin production, dimethyl sulfide and dimethyl sulfoxide production, phenol substitute in phenolic resins incorporation into polyolefin blends, aromatic (phenol) monomers, additional miscellaneous monomers, carbon fibers, metal sequestration in solutions, basis of gel formation, polyurethane copolymer - as a renewable filler/extender, and the like. [0050] 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. EXAMPLES Example 1: Preparation of lignin compositions [0051] Lignin compositions of the invention were prepared using supercritical, subcritical, and near critical water extraction in a two stage process. Particulate 12 WO 2013/101397 PCT/US2012/067535 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 about 170-245'C and then feed into a pretreatment reactor for about 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 0 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 about 150-250'C. The slurry was then subjected to supercritical water at about 374-600*C in a hydrolysis reactor for about 0.05-10 seconds under a pressure of about 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. Example 2: Analysis of lignin compositions using inductively coupled plasma [0052] The dried compositions containing the lignin of Example 1 were analyzed using inductively coupled plasma emission spectroscopy. The results are shown in the table below: Sample Duplicate Sample Duplicate Sample Duplicate IPA ReotdB Reotdc Reorted element Reported Rorte Reported Repotd p Reported Rep Average conc. Coonc . n.Conc. oc (mg/kg) (mg/kg) mg/kg) (mg/kg) (mg/kg) (mg/kg) (mg/kg) _________________________________ Al 45.5 47.8 39.1 37.5 43.6 40.4 42.3 As < 12.6 < 14.6 < 12.1 < 12.5 < 13.6 < 15.6 13.5 B 3.22 0.777 2.88 1.66 0.603 < 0.605 1.6 Ba 3.34 3.62 2.99 2.99 3.02 2.77 3.1 Be < 0.0300 < 0.0349 < 0.0288 < 0.0299 < 0.0326 < 0.0374 0.0 Ca 618 671 551 535 594 545 585.7 Cd < 0.667 < 0.777 < 0.640 < 0.665 < 0.724 < 0.830 0.7 Co < 0.972 < 1.13 < 0.933 < 0.969 < 1.05 < 1.21 1.0 Cr 1.56 1.94 1.60 1.66 1.33 1.38 1.6 Cu 5.89 8.80 7.26 7.87 6.64 19.0 9.2 Fe 465 501 313 298 351 320 374.6 K 39.1 40.4 23.7 31.1 33.1 44.1 35.3 Li < 0.245 < 0.285 < 0.235 < 0.244 < 0.266 < 0.304 0.3 Mg 21.9 22.1 18.8 19.0 18.6 19.8 20.0 Mn 5.89 6.47 5.02 4.99 4.34 4.01 5.1 Mo < 2.34 < 2.72 < 2.25 < 2.33 < 2.54 < 2.91 2.5 Na 58.7 52.0 54.6 40.7 50.6 61.0 52.9 13 WO 2013/101397 PCT/US2012/067535 Sample Duplicate Sample Duplicate Sample Duplicate lCP A ReotdB Ceore ceorted element Reported Rorte Reported Reponcd Reported Rep Average Con.nc.kg Conc. Conc.g Conc. Conc.g (mg/kg) (mg/kg) mg/kg) (mg/kg) (mg/kg) (mg/kg) Ni < 1.16 < 1.35 < 1.12 < 1.16 < 1.26 < 1.45 1.3 P < 89.9 < 105 < 86.2 < 89.6 < 97.5 < 112 96.6 Pb < 7.95 < 9.25 < 7.63 < 7.92 < 8.63 < 9.89 8.5 S 105 132 146 128 128 103 123.6 Sb < 7.46 < 8.68 < 7.16 < 7.43 < 8.09 < 9.28 8.0 Se < 16.5 < 19.2 < 15.9 < 16.5 < 18.0 < 20.6 17.8 Si 54.9 63.9 42.1 57.2 67.6 64.5 58.4 Sn 9.23 9.19 7.04 7.65 10.9 10.1 9.0 Sr 2.11 2.20 1.81 1.77 1.93 1.80 1.9 Ti 3.56 5.57 2.77 5.87 3.26 3.46 4.1 TI < 16.7 < 19.5 < 16.1 < 16.7 < 18.2 < 20.8 18.0 V < 0.260 < 0.303 < 0.250 0.332 < 0.282 < 0.324 0.3 Zn 9.79 11.0 9.28 9.86 7.48 6.37 9.0 Total Elements 1610.3 1762.1 1378.7 1347.2 1496.6 1441.4 1506.0 Example 3: Analysis of lignin for carbon, hydrogen, and nitrogen [0053] Dried compositions containing lignin were analyzed to determine the levels of ash, carbon, hydrogen, and nitrogen by thermal conductivity detection after combustion and reduction. The results are shown in the table below: Element/Material Sample 1 Sample 2 C 56.76% 57.09% H 5.46% 5.66% N 0.18% 0.19% Ash 1.1% 1.1% Ratio of N+H:C 0.099 0.102 Example 4: Lignin Characterization [0054] The NREL method for lignin (acid hydrolysis followed by gravimetric protocol in accordance with standard NREL procedures found at http:/Iwww. nrel.ciov/biomass/pdfs/42618.pdf and pyrolysis molecular beam mass spectrometry (py MBMS) were used to quantify the level of lignin in the solids, using lignin from hardwood as a standard. The results are shown in the table below: 14 WO 2013/101397 PCT/US2012/067535 Sample Lignin Weight % Lignin Weight % Syringyl/Guaiacyl from NREL Method from py-MBMS Weight Ratio from Method py-MBMS Method Hardwood 28 23.3 2.6 standard Pretreated 40-44 21.6 2.4 solids Solid residue >50 33.3 2.5 after supercritical hydrolysis [0055] 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. [0056] The disclosures of each patent, patent application, and publication cited or described in this document are hereby incorporated herein by reference, in their entirety. [0057] 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. 15
权利要求:
Claims (27)
[1] 1. A composition, comprising: lignin; and less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn.
[2] 2. A composition of claim 1, wherein said lignin has a heating value as measured by ASTM-D240 and D5865 of at least about 5,000 BTU/lb.
[3] 3. A composition of claim 1, wherein said lignin has an average particle size less than about 500 microns.
[4] 4. A composition of claim 1, wherein said lignin has a bulk density of less than about 0.35 g/cc.
[5] 5. A composition of claim 1, wherein said lignin is processed from lignocellulosic biomass optionally using supercritical, subcritical, or near critical fluid extraction or combinations thereof.
[6] 6. A composition of claim 1, wherein said composition is substantially free of organic solvent.
[7] 7. A composition of claim 1, wherein said lignin is in a powdered form.
[8] 8. A composition of claim 1, wherein said lignin is in a pelletized form. 16 WO 2013/101397 PCT/US2012/067535
[9] 9. A composition of claim 1, wherein said lignin is in a liquid form.
[10] 10. A composition of claim 1, further comprising: less than about 700 mg of calcium per kg of said lignin.
[11] 11. A composition of claim 1, further comprising: less than about 525 mg of iron per kg of said lignin.
[12] 12. A composition of claim 1, further comprising: less than about 150 mg of sulfur per kg of said lignin.
[13] 13. A composition of claim 1, wherein levels of said elements are measured by inductively coupled plasma emission spectroscopy.
[14] 14. A composition of claim 1, further comprising: less than about 20 g of ash per kg of said lignin.
[15] 15. A composition of claim 1, further comprising: less than about 2000 mg of nitrogen per kg of said lignin.
[16] 16. A composition of claim 1, further comprising: a weight ratio of the total mass of hydrogen and nitrogen to carbon of less than about 0.110.
[17] 17. A composition of claim 1, wherein said lignin is present at a level of at least 30% by weight, based on the total weight of the composition, as measured by pyrolysis molecular beam mass spectrometry. 17 WO 2013/101397 PCT/US2012/067535
[18] 18. A composition of claim 1, wherein the weight ratio of syringyl monolignol to guaiacyl monolignol is about 2.0 to about 3.0, as measured by pyrolysis molecular beam mass spectrometry.
[19] 19. A composition, comprising: lignin; less than about 700 mg of calcium per kg of said lignin; less than about 525 mg of iron per kg of said lignin; and less than about 150 mg of sulfur per kg of said lignin.
[20] 20. A composition of claim 19, further comprising: less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn.
[21] 21. A composition, comprising: lignin; and less than about 525 mg of iron per kg of said lignin.
[22] 22. A composition of claim 21, further comprising: less than about 700 mg of calcium per kg of said lignin.
[23] 23. A composition of claim 21, further comprising: less than about 2000 mg in total per kg of said lignin of elements; wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn.
[24] 24. A composition, comprising: lignin; and less than about 150 mg of sulfur per kg of said lignin.
[25] 25. A composition of claim 24, further comprising: less than about 2000 mg in total per kg of said lignin of elements; 18 WO 2013/101397 PCT/US2012/067535 wherein said elements are Al, As, B, Ba, Be, Ca, Cd, Co, Cr, Cu, Fe, K, Li, Mg, Mn, Mo, Na, Ni, P, Pb, S, Sb, Se, Si, Sn, Sr, Ti, TI, V, and Zn.
[26] 26. A composition of claim 24, further comprising: less than about 700 mg of calcium per kg of said lignin.
[27] 27. A composition of claim 24, further comprising: less than about 525 mg of iron per kg of said lignin. 19
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同族专利:
公开号 | 公开日
MY167811A|2018-09-26|
US9255188B2|2016-02-09|
SG10201610518QA|2017-02-27|
US20140039144A1|2014-02-06|
BR112014015905A8|2017-07-04|
WO2013101397A1|2013-07-04|
JP2015504111A|2015-02-05|
PH12014501323B1|2014-09-15|
US8759498B2|2014-06-24|
CA2859752A1|2013-07-04|
RU2629062C2|2017-08-24|
RU2012154209A|2014-06-20|
US9963555B2|2018-05-08|
KR20140116875A|2014-10-06|
JP6083763B2|2017-02-22|
US20160108182A1|2016-04-21|
US20130172540A1|2013-07-04|
PH12014501323A1|2014-09-15|
CA2859752C|2020-03-24|
AU2012362936B2|2016-07-07|
BR112014015905A2|2017-06-13|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题
US9963555B2|2011-12-30|2018-05-08|Renmatix, Inc.|Compositions comprising lignin|
US10053745B2|2010-01-19|2018-08-21|Renmatix, Inc.|Production of fermentable sugars and lignin from biomass using supercritical fluids|US1783163A|1925-09-26|1930-11-25|Dow Chemical Co|Pressure-relieving method and apparatus for autoclaves and the like|
GB291991A|1927-08-19|1928-06-14|Corn Prod Refining Co|Manufacture of dextrose|
US1959433A|1931-02-11|1934-05-22|Emil C Loetscher|Water-soluble resins of the phenol formaldehyde group|
US1938802A|1932-04-19|1933-12-12|Chemipulp Process Inc|Continuous process and apparatus for pulping fibrous materials|
US2198785A|1937-06-07|1940-04-30|Mohr John|Method for treating waste materials|
US2156159A|1938-05-17|1939-04-25|Northwood Chemical Company|Process of making lignin|
US2356500A|1941-03-27|1944-08-22|Boinot Firmin Charles|Method for saccharifying cellulosic materials by means of diluted mineral acids|
US2516833A|1947-06-09|1950-08-01|Ant-Wuorinen Olli Viljo Anton|Process for hydrolyzing cellulosic materials|
US2681871A|1951-02-16|1954-06-22|Sam M Nickey Jr|Method and apparatus for hydrolyzing cellulosic materials|
GB692284A|1951-03-05|1953-06-03|Union Starch And Refining Comp|Stable syrup of high dextrine content and method of manufacturing same|
US2759856A|1952-11-05|1956-08-21|Masonite Corp|Preparation of high purity wood sugars|
US2781328A|1953-05-06|1957-02-12|Agrashell Inc|Phenolic resin glue compositions containing hydrolyzed ligno-cellulosic degradation products|
US2727869A|1953-06-12|1955-12-20|Monsanto Chemicals|Phenolic adhesive and method of making same|
US2851382A|1954-05-05|1958-09-09|Walter L Schmidt|Method for hydrolyzing cellulosic materials|
US2801939A|1955-04-04|1957-08-06|Tennessee Valley Authority|Hydrolysis of hemicellulose and alphacellulose to produce sugar|
US2810394A|1955-04-08|1957-10-22|Ferguson Robert Eugene|Valve construction|
US2822784A|1955-05-09|1958-02-11|Babcock & Wilcox Co|Apparatus for and method of generating and superheating vapor|
US2881783A|1956-07-11|1959-04-14|Exxon Research Engineering Co|Self-cleaning valve|
US2994633A|1958-08-21|1961-08-01|Crossett Company|Process for separating lignin solids from used neutral sulfite pulping liquors|
US2997466A|1958-11-04|1961-08-22|West Virginia Pulp & Paper Co|Decantation of lignin|
US3294715A|1962-08-01|1966-12-27|Dow Chemical Co|Phenolic resin adhesive extended withcausticized lignite|
US3212932A|1963-04-12|1965-10-19|Georgia Pacific Corp|Selective hydrolysis of lignocellulose materials|
US3314797A|1963-04-12|1967-04-18|Georgia Pacific Corp|Converting lignocellulose materials into yeast containing stock feed|
GB1245486A|1969-12-04|1971-09-08|Sued Chemie Ag|Process for the preparation of xylose solutions|
US3792719A|1971-10-20|1974-02-19|Westinghouse Electric Corp|Self-cleaning flow restricting device|
DE2413306B2|1973-05-04|1976-09-30|Gebrüder Sulzer AG, Winterthur |METHOD OF PREPARING XYLOSE SOLUTION|
JPS5630000B2|1974-05-17|1981-07-11|||
DE2545111C3|1975-10-08|1980-07-17|Sued-Chemie Ag, 8000 Muenchen|Process for the two-stage digestion of xylan-containing natural products for the purpose of obtaining xylose|
CA1079008A|1975-10-24|1980-06-10|Cp Associates Limited|Solvent pulping process|
ZA766073B|1975-10-24|1977-09-28|D Econimidis|Production of pulp|
US3990904A|1976-05-11|1976-11-09|Sud-Chemie Ag|Method for the preparation of xylose solutions|
DE2737118C2|1977-08-17|1989-06-15|Bau- Und Forschungsgesellschaft Thermoform Ag, Murten, Fribourg, Ch||
CA1100266A|1977-08-31|1981-05-05|Laszlo Paszner|Organosolv delignification and saccharification process for lignocellulosic plant materials|
US4470851A|1981-03-26|1984-09-11|Laszlo Paszner|High efficiency organosolv saccharification process|
US5628830A|1979-03-23|1997-05-13|The Regents Of The University Of California|Enzymatic hydrolysis of biomass material|
US4201596A|1979-01-12|1980-05-06|American Can Company|Continuous process for cellulose saccharification|
US5366558A|1979-03-23|1994-11-22|Brink David L|Method of treating biomass material|
FR2462433A1|1979-08-03|1981-02-13|Bertin & Cie|IMPROVEMENTS IN PROCESSES AND EQUIPMENT FOR OBTAINING FURFURAL FROM PLANT MATERIALS|
JPS5847213B2|1979-09-20|1983-10-21|Kogyo Gijutsuin||
CA1173380A|1980-02-19|1984-08-28|Michael I. Sherman|Acid hydrolysis of biomass for ethanol production|
FI810523L|1980-02-23|1981-08-24|Franz Johann Reitter|REQUIREMENTS FOR CONTAINING CONTAINER HYDROLYS AV CELLULOSAHALTIG VAEXT-BIOSUBSTANS FOER UTVINNING AV SOCKER|
US4363671A|1980-03-18|1982-12-14|New York University|Apparatus for chemical conversion of materials|
CA1190923A|1980-03-18|1985-07-23|Barry Rugg|Process and apparatus for chemical conversion ofmaterials and particularly the conversion ofcellulose waste to glucose|
US4368079A|1980-03-18|1983-01-11|New York University|Apparatus for chemical conversion of materials and particularly the conversion of cellulose waste to glucose|
US4316748A|1980-03-18|1982-02-23|New York University|Process for the acid hydrolysis of waste cellulose to glucose|
US4316747A|1980-03-18|1982-02-23|New York University|Process for the chemical conversion of cellulose waste to glucose|
US4318748A|1980-04-09|1982-03-09|American Can Company|Continuous process for saccharification of whole starchy materials|
US4543190A|1980-05-08|1985-09-24|Modar, Inc.|Processing methods for the oxidation of organics in supercritical water|
US4338199B1|1980-05-08|1988-11-15|||
US4308200A|1980-07-10|1981-12-29|Champion International Corporation|Extraction of coniferous woods with fluid carbon dioxide and other supercritical fluids|
JPS5761083A|1980-09-30|1982-04-13|Kobe Steel Ltd|Pressure reduction liquefaction reactor in coal|
DE3048802A1|1980-12-23|1982-07-08|Werner & Pfleiderer, 7000 Stuttgart|METHOD FOR THE HYDROLYSIS OF CELLULOSE VEGETABLE RAW MATERIALS TO GLUCOSE AND DEVICE FOR IMPLEMENTING THE METHOD|
US4357194A|1981-04-14|1982-11-02|John Stofko|Steam bonding of solid lignocellulosic material|
CS225851B1|1981-05-04|1984-03-19|Jozef Doc Ing Csc Pajtik|Method of treating wood and other ligno-cellulosic raw materials by prehydrolysing and fibrillating,or delignifying for further processing|
WO1983000370A1|1981-07-27|1983-02-03|Pittsburgh Midway Coal Mining|Apparatus and method for let down of a high pressure abrasive slurry|
JPS6260602B2|1981-08-28|1987-12-17|Hitachi Ltd||
DK522881A|1981-11-25|1983-05-26|Danske Sukkerfab|PROCEDURE FOR THE CONVERSION OF A PENTOSHOLD CELLULOS MATERIAL FOR XYLOSE AND GLUCOSE BY ACID HYDROLYSE|
US4405377A|1982-02-10|1983-09-20|Uop Inc.|Process for the separation of monosaccharides|
CS248106B1|1982-04-05|1987-01-15|Jan Hojnos|Method of acid prehydrolysis of wooden spears|
EP0098490B1|1982-07-05|1989-01-25|Erne-Fittings Gesellschaft M.B.H. & Co.|Process and apparatus for the preparation of cellulose, simple sugars and soluble lignine from vegetable biomasse|
DE3225074A1|1982-07-05|1984-01-12|Josef Erne & Co, Rohrbogenwerk, 6824 Schlins|Process and device for separating hemicellulose and lignin from cellulose in lignocellulosic plant materials, for obtaining cellulose, optionally sugars and optionally soluble lignin|
SU1086046A1|1982-07-12|1984-04-15|Ленинградская Ордена Ленина Лесотехническая Академия Им.С.М.Кирова|Wood delignification method|
US4556430A|1982-09-20|1985-12-03|Trustees Of Dartmouth College|Process for hydrolysis of biomass|
US4674285A|1983-05-16|1987-06-23|The Babcock & Wilcox Company|Start-up control system and vessel for LMFBR|
DE3428661C2|1983-08-09|1988-01-28|Fried. Krupp Gmbh, 4300 Essen, De||
US4493797A|1983-12-22|1985-01-15|Domtar Inc|Apparatus and method involving supercritical fluid extraction|
CA1198703A|1984-08-02|1985-12-31|Edward A. De Long|Method of producing level off d p microcrystallinecellulose and glucose from lignocellulosic material|
US4675198A|1984-12-31|1987-06-23|The Procter & Gamble Co.|Removal of textured vegetable product off-flavor by supercritical fluid or liquid extraction|
FR2580669B1|1985-04-18|1987-09-18|Inst Francais Du Petrole|PROCESS FOR CONVERTING LIGNOCELLULOSIC SUBSTRATES INTO PENTOSES|
US4607819A|1985-05-07|1986-08-26|Spils Richard W|High pressure radial flow valve|
US4644060A|1985-05-21|1987-02-17|E. I. Du Pont De Nemours And Company|Supercritical ammonia treatment of lignocellulosic materials|
US4699124A|1985-06-28|1987-10-13|Power Alcohol, Inc.|Process for converting cellulose to glucose and other saccharides|
US4637835A|1985-06-28|1987-01-20|Power Alcohol, Inc.|Methods of hydrolyzing cellulose to glucose and other saccharides|
US4764596A|1985-11-05|1988-08-16|Repap Technologies Inc.|Recovery of lignin|
US5788812A|1985-11-05|1998-08-04|Agar; Richard C.|Method of recovering furfural from organic pulping liquor|
JPS62283988A|1986-06-02|1987-12-09|Hitachi Ltd|Production of maltooligosaccharide|
CA1284637C|1987-08-24|1991-06-04|George S. Faass|Biomass fractionation process|
JP2595308B2|1987-09-04|1997-04-02|王子製紙株式会社|Lignin-phenol resin composition|
US4857638A|1987-12-28|1989-08-15|Domtar Inc.|Lignin having nitrogen and sulfur and process therefor employing thiourea|
US5169687A|1988-09-16|1992-12-08|University Of South Florida|Supercritical fluid-aided treatment of porous materials|
US5041192A|1988-09-16|1991-08-20|University Of South Florida|Supercritical delignification of wood|
EP0364632A1|1988-10-17|1990-04-25|Zeneca Limited|Production of lignin|
US4964995A|1989-06-16|1990-10-23|Midwest Research Institute|Supercritical separation process for complex organic mixtures|
US5196460A|1990-05-29|1993-03-23|Repap Technologies Inc.|Rubber compositions containing high purity lignin derivatives|
US5009746A|1990-10-12|1991-04-23|Kimberly-Clark Corporation|Method for removing stickies from secondary fibers using supercritical CO2 solvent extraction|
US5213660A|1990-10-12|1993-05-25|Kimberly-Clark Corporation|Secondary fiber cellulose product with reduced levels of polychlorinated dibenzodioxins and polychlorinated dibenzofurans|
JPH04197192A|1990-11-29|1992-07-16|Kirin Brewery Co Ltd|Production of xylose and reduced xylose|
US5125977A|1991-04-08|1992-06-30|The United States Of America As Represented By The United States Department Of Energy|Two-stage dilute acid prehydrolysis of biomass|
US5411594A|1991-07-08|1995-05-02|Brelsford; Donald L.|Bei hydrolysis process system an improved process for the continuous hydrolysis saccharification of ligno-cellulosics in a two-stage plug-flow-reactor system|
DE4228897A1|1992-08-29|1994-03-03|Wella Ag|Hair setting agent based on lignin or lignin derivatives and dihydroxypropyllignin|
US5328934A|1992-10-27|1994-07-12|Hoechst Celanese Corporation|Recycling cellulose esters from the waste from cigarette manufacture|
US5338366A|1993-01-04|1994-08-16|Kamyr, Inc.|Acid pre-hydrolysis reactor system|
US5384051A|1993-02-05|1995-01-24|Mcginness; Thomas G.|Supercritical oxidation reactor|
US6569640B1|1993-03-12|2003-05-27|Aphios Corporation|Method of fractionation of biologically-derived materials using critical fluids|
US5516952A|1993-08-11|1996-05-14|The University Of Akron|Oxidative decoupling of scrap rubber|
US5705369A|1994-12-27|1998-01-06|Midwest Research Institute|Prehydrolysis of lignocellulose|
US5424417A|1993-09-24|1995-06-13|Midwest Research Institute|Prehydrolysis of lignocellulose|
US5824187A|1993-12-29|1998-10-20|Kvaerner Pulping Ab|Method for the continuous cooking of pulp|
US5512231A|1995-01-26|1996-04-30|Hoechst Celanese Corporation|Processing cellulose acetate formed articles using supercritical fluid|
FI952065A0|1995-03-01|1995-04-28|Xyrofin Oy|Foilfarande Foer tillvaratagande av en kristalliserbar organisk foerening|
JP3024526B2|1995-10-11|2000-03-21|日本製紙株式会社|Lignin composition, method for producing the same, and cement dispersant using the same|
JPH11513726A|1995-10-18|1999-11-24|アルセルテクノロジーズインコーポレイテッド|Lignin based friction material|
US5615708A|1995-10-23|1997-04-01|Fisher Controls International, Inc.|Flow control valve with non-plugging multi-stage valve trim|
US6025452A|1996-12-27|2000-02-15|Kurple; Kenneth R.|Lignin based polyols|
JP4197192B2|1996-09-20|2008-12-17|株式会社ニコン|Image playback device|
US6022419A|1996-09-30|2000-02-08|Midwest Research Institute|Hydrolysis and fractionation of lignocellulosic biomass|
US6228177B1|1996-09-30|2001-05-08|Midwest Research Institute|Aqueous fractionation of biomass based on novel carbohydrate hydrolysis kinetics|
DE69710748T2|1996-10-18|2002-08-22|Kronospan Gmbh|TREATMENT OF LIGNOCELLULOSE MATERIALS|
US5830763A|1996-11-06|1998-11-03|Junk; Thomas|Process for preparing deuterium tagged compounds|
US6090291A|1997-08-20|2000-07-18|Kabushiki Kaisha Toshiba|Waste processing method and waste processing apparatus|
RU2109059C1|1997-10-30|1998-04-20|Блинков Сергей Дмитриевич|Method of processing vegetable raw material to produce pentose hydrolyzates predominantly containing xylose|
JP4843125B2|1998-02-13|2011-12-21|木村化工機株式会社|Pressure control mechanism of slurry liquid high temperature and high pressure reaction treatment system|
AU4700199A|1998-06-23|2000-01-10|Regents Of The University Of California, The|Method of treating biomass material|
DE19905655A1|1999-02-11|2000-08-17|Karl Zeitsch|Process for the production of furfural by delayed relaxation|
CA2627846C|1999-03-23|2011-01-04|Oji Paper Co., Ltd.|Process for bleaching lignocellulose pulp|
DE19916347C1|1999-04-12|2000-11-09|Rhodia Acetow Ag|Process for separating biomass containing lignocellulose|
DE19917178A1|1999-04-16|2000-10-19|Karl Zeitsch|Production of furfural from sulfite waste liquor involves heating by direct injection of steam, reaction by boiling under pressure, using easily separated ancillary, and complete vaporization by cooling and depressurization|
BR9902607B1|1999-06-23|2010-08-24||biomass pre-hydrolysis apparatus and process.|
US20020069987A1|2000-08-08|2002-06-13|Pye Edward Kendall|Integrated processing of biomass and liquid effluents|
JP2001095594A|1999-09-30|2001-04-10|Meiji Seika Kaisha Ltd|Production of glucose and cellooligosaccharide|
US6180845B1|1999-10-07|2001-01-30|Board Of Supervisors Of Louisiana State University And Agricultural And Mechanical College|Transforming biomass to hydrocarbon mixtures in near-critical or supercritical water|
WO2001032715A1|1999-11-02|2001-05-10|Waste Energy Integrated Sytems, Llc|Process for the production of organic products from lignocellulose containing biomass sources|
CA2400336C|2000-02-17|2010-04-27|Forskningscenter Riso|A method for processing lignocellulosic material|
JP4533496B2|2000-03-15|2010-09-01|三菱重工業株式会社|Fuel production method from biomass|
AU4831501A|2000-03-16|2001-09-24|Bioconsult Ges Fur Biotechnolo|Sulphur-free lignin and derivatives thereof for reducing the formation of slime and deposits in industrial plants|
CA2404029A1|2000-03-23|2001-09-27|Richard W. Russell|Method of converting agricultural waste to liquid fuel and associated apparatus|
US6612317B2|2000-04-18|2003-09-02|S.C. Fluids, Inc|Supercritical fluid delivery and recovery system for semiconductor wafer processing|
JP4083374B2|2000-07-11|2008-04-30|トヨタ自動車株式会社|Method for producing cellulose|
US6419788B1|2000-08-16|2002-07-16|Purevision Technology, Inc.|Method of treating lignocellulosic biomass to produce cellulose|
EP1184443A1|2000-09-04|2002-03-06|Biofuel B.V.|Process for the production of liquid fuels from biomass|
FR2813599B1|2000-09-07|2003-05-16|Centre Nat Rech Scient|PROCESS FOR TREATING WASTE BY HYDROTHERMAL OXIDATION|
JP3912023B2|2000-09-25|2007-05-09|日本製紙株式会社|Biodegradable composition and method for producing the same|
FI111960B|2000-12-28|2003-10-15|Danisco Sweeteners Oy|separation Process|
AU2002234469B2|2001-02-28|2007-07-19|Iogen Energy Corporation|Method of processing lignocellulosic feedstock for enhanced xylose and ethanol production|
JP4683748B2|2001-03-07|2011-05-18|ヤンマー株式会社|Reactor reaction equipment with supercritical water or subcritical water|
DE10158120A1|2001-11-27|2003-06-18|Ties Karstens|Process for separating xylose from xylan-rich lignocelluloses, especially wood|
JP4330839B2|2002-01-18|2009-09-16|旭化成ケミカルズ株式会社|Method for producing glucose and / or water-soluble cellooligosaccharide|
DE10207257B4|2002-02-21|2021-02-18|Kennametal Inc.|Rotary cutting tool with exchangeable cutting insert|
US7189306B2|2002-02-22|2007-03-13|Gervais Gibson W|Process of treating lignocellulosic material to produce bio-ethanol|
AU2003256788A1|2002-07-25|2004-02-23|Coffin World Water Systems|Apparatus and method for treating black liquor|
US6896810B2|2002-08-02|2005-05-24|Rayonier Products And Financial Services Company|Process for producing alkaline treated cellulosic fibers|
GB0218012D0|2002-08-05|2002-09-11|Ciba Spec Chem Water Treat Ltd|Production of a fermentation product|
DE10259928B4|2002-12-20|2006-05-24|Forschungszentrum Karlsruhe Gmbh|Process for the treatment of biomass|
US8003833B2|2003-03-28|2011-08-23|Ab-Cwt, Llc|Process for conversion of organic, waste, or low-value materials into useful products|
BR0301678A|2003-06-10|2005-03-22|Getec Guanabara Quimica Ind S|Process for the production of crystalline xylose from sugarcane bagasse, high purity crystalline xylose produced by said process, process for the production of crystalline xylitol from the high purity crystalline xylose and thus obtained|
JP4277603B2|2003-07-24|2009-06-10|日立造船株式会社|Method for hydrolysis of polysaccharide substances|
US20070267008A1|2003-11-21|2007-11-22|Tama-Tlo Corporation|Method of Hydrolyzing an Organic Compound|
CN1303091C|2004-04-05|2007-03-07|山东龙力生物科技有限公司|Preparation of oligo-wood sugar|
JP2007532587A|2004-04-13|2007-11-15|アイオゲン エナジー コーポレイション|Inorganic salt recovery method in lignocellulose treatment|
JP4982036B2|2004-04-16|2012-07-25|志朗 坂|Biomass decomposition and liquefaction method|
WO2006007691A1|2004-07-16|2006-01-26|Iogen Energy Corporation|Method of obtaining a product sugar stream from cellulosic biomass|
EA011136B1|2004-08-31|2008-12-30|Биотек Прогресс, А.С.|Method and devices for continuous processing of renewable raw materials|
DK176540B1|2004-09-24|2008-07-21|Cambi Bioethanol Aps|Process for the treatment of biomass and organic waste in order to extract desired biologically based products|
SE0402437D0|2004-10-07|2004-10-07|Stfi Packforsk Ab|Method for separating lignin from a lignin containing liquid / slurry|
US7259231B2|2004-10-12|2007-08-21|Yulex Corporation|Extraction and fractionation of biopolymers and resins from plant materials|
US7722823B2|2004-10-22|2010-05-25|Drs Sustainment Systems, Inc.|Systems and methods for air purification using supercritical water oxidation|
US20070161095A1|2005-01-18|2007-07-12|Gurin Michael H|Biomass Fuel Synthesis Methods for Increased Energy Efficiency|
JP2006223152A|2005-02-16|2006-08-31|Hitachi Zosen Corp|Method for treating biomass through combination of dissolution by cellulose solvent and hydrolysis|
JP2006255676A|2005-03-18|2006-09-28|Kri Inc|Method for separating lignin substance|
JP4651086B2|2005-03-22|2011-03-16|トヨタ自動車株式会社|Cellulose degradation method|
US7964761B2|2005-05-02|2011-06-21|University Of Utah Research Foundation|Processes for catalytic conversion of lignin to liquid bio-fuels and novel bio-fuels|
US7754457B2|2005-06-03|2010-07-13|Iogen Energy Corporation|Method of continuous processing of lignocellulosic feedstock|
US7566383B2|2005-06-17|2009-07-28|Purdue Research Foundation|Heat recovery from a biomass heat source|
ES2606281T3|2005-07-19|2017-03-23|Inbicon A/S|Method and apparatus for the conversion of cellulosic material into ethanol|
CN101272794B|2005-09-27|2015-08-26|旭化成化学株式会社|Compositions containing cell-oligosaccharide|
AR057141A1|2005-09-28|2007-11-21|Cwt Llc Ab|DEPOLIMERIZATION PROCESSING TO CONVERT ORGANIC AND NON-ORGANIC WASTE PRODUCTS IN USEFUL PRODUCTS|
CA2628591A1|2005-11-04|2007-05-18|Pandora Select Partners, L.P.|Nutrient extracts derived from green plant materials|
US7914668B2|2005-11-14|2011-03-29|Exxonmobil Research & Engineering Company|Continuous coking process|
US20090176286A1|2005-11-23|2009-07-09|O'connor Ryan P|Process for Fractionating Lignocellulosic Biomass into Liquid and Solid Products|
EP2007945B1|2006-03-29|2011-01-26|Virginia Tech Intellectual Properties, Inc.|Cellulose-solvent-based lignocellulose fractionation with modest reaction conditions and reagent cycling|
US20070254348A1|2006-04-28|2007-11-01|Theodora Retsina|Method for the production of fermentable sugars and cellulose from lignocellulosic material|
MY148779A|2006-05-08|2013-05-31|Vertichem Corp|Integrated processing of plant biomass|
JP4666378B2|2006-05-29|2011-04-06|パナソニック株式会社|Decomposition method for woody waste|
US8765938B2|2006-06-26|2014-07-01|Tokyo Institute Of Technology|Process for production of polysaccharide and/or monosaccharide by hydrolysis of different polysaccharide|
JP4765073B2|2006-07-05|2011-09-07|国立大学法人広島大学|Method for hydrothermal hydrolysis of lignocellulose|
JP5190858B2|2006-07-12|2013-04-24|独立行政法人農業・食品産業技術総合研究機構|Production method of low molecular weight carbohydrates from materials containing polysaccharides|
US20080029233A1|2006-08-03|2008-02-07|Purevision Technology, Inc.|Moving bed biomass fractionation system and method|
CN101522760A|2006-08-07|2009-09-02|艾米塞莱克斯能源公司|Process for recovery of holocellulose and near-native lignin from biomass|
NO20063872A|2006-08-30|2008-01-14|Cambi As|Method for thermal enzymatic hydrolysis of lignocellulose|
NZ575879A|2006-09-01|2012-09-28|Ra Energy Corp|Advanced biorefinery process|
US7666637B2|2006-09-05|2010-02-23|Xuan Nghinh Nguyen|Integrated process for separation of lignocellulosic components to fermentable sugars for production of ethanol and chemicals|
CN1931866A|2006-09-29|2007-03-21|张海龙|Process of producing xylose with stalks|
US7670813B2|2006-10-25|2010-03-02|Iogen Energy Corporation|Inorganic salt recovery during processing of lignocellulosic feedstocks|
ES2545754T3|2006-10-26|2015-09-15|Kawasaki Jukogyo Kabushiki Kaisha|Method and system for hydrolytic saccharification of a cellulosic biomass|
WO2008063549A2|2006-11-17|2008-05-29|Summerhill Biomass Systems, Inc.|Powdered fuels, dispersions thereof, and combustion devices related thereto|
US20090223612A1|2007-11-16|2009-09-10|Mcknight James K|Powdered fuels and powdered fuel dispersions|
CN104445077A|2006-12-16|2015-03-25|克里斯多佛·J·帕皮雷|Consuming carbon dioxide to generate heat so as to assist zero-emission power generation|
CA2674534A1|2007-01-23|2008-07-31|Basf Se|Method for producing glucose by enzymatic hydrolysis of cellulose that is obtained from material containing ligno-cellulose using an ionic liquid that comprises a polyatomic anion|
SE531491C2|2007-03-29|2009-04-28|Reac Fuel Ab|Fuel produced from biomass|
JP2008248202A|2007-03-30|2008-10-16|Toyota Motor Corp|Method and apparatus for purifying cellulose|
WO2008137639A1|2007-05-02|2008-11-13|Mascoma Corporation|Two-stage method for pretreatment of lignocellulosic biomass|
JP4284471B2|2007-05-22|2009-06-24|国立大学法人東北大学|Supercritical water biomass fired boiler|
RU2338769C1|2007-05-22|2008-11-20|Институт физической химии и электрохимии им. А.Н. Фрумкина Российской академии наук|Method of processing plant raw material|
US9260818B2|2007-05-23|2016-02-16|Andritz Inc.|Single vessel reactor system for hydrolysis and digestion of wood chips with chemical enhanced wash method|
US8734610B2|2007-05-23|2014-05-27|Andritz Inc.|Two vessel reactor system and method for hydrolysis and digestion of wood chips with chemical enhanced wash method|
BRPI0810953A2|2007-05-23|2014-10-14|Tate & Lyle Ingredientes Americas Inc|EDIBLE COMPOSITION, FOOD PRODUCT, METHOD FOR REDUCING THE GLYCEMIC RESPONSE OF A MAMMAL TO A FOOD PRODUCT, SWEET COMPOSITION PACKED FOR SINGLE PORTION, MAKING SYRUP COMPOSITION, ADDICTIVE ADDICTION COMPOSITION .|
US8193324B2|2007-05-31|2012-06-05|Lignol Innovations Ltd.|Continuous counter-current organosolv processing of lignocellulosic feedstocks|
RU2482908C2|2007-07-27|2013-05-27|Игнайт Энерджи Ресорсиз Пти Лтд|Method and device for converting organic material into product|
WO2009015614A1|2007-07-30|2009-02-05|Kmps Financial Group, S.R.O.|Method and equipment for production of glucose, ethanol, furfural, furane and lignin from renewable raw materials|
WO2009021216A2|2007-08-08|2009-02-12|Bountiful Applied Research Corp.|Lignin dewatering process|
WO2009029344A1|2007-08-27|2009-03-05|Endicott Biofuels Ii, Llc|Production of ester-based fuels such as biodiesel from renewable starting materials|
NZ598528A|2007-08-31|2013-08-30|Vertichem Corp|Lignin and other products isolated from plant material, and methods and compositions therefor|
KR20090030967A|2007-09-21|2009-03-25|대한민국|Saccharification method of wood biomasses using supercritical water|
US8585863B2|2007-09-21|2013-11-19|Api Intellectual Property Holdings, Llc|Separation of lignin from hydrolyzate|
KR20090039470A|2007-10-18|2009-04-22|대한민국|Saccharification of woody biomasses using supercritical water in presence of acid catalysts|
WO2009058276A1|2007-11-01|2009-05-07|Mascoma Corporation|Product recovery from fermentation of lignocellulosic biomass|
FI121885B|2007-11-09|2011-05-31|Chempolis Oy|A process for making a sugar product|
CN101200479B|2007-12-20|2010-08-25|武汉工程大学|Method for reclaiming xylose from waste liquor of cellulose raw material pretreated by dilute acid|
US20100330638A1|2008-02-12|2010-12-30|Aita Giovanna M|Thermochemical Treatment of Lignocellulosics for the Production of Ethanol|
JP5322150B2|2008-02-14|2013-10-23|独立行政法人農業・食品産業技術総合研究機構|Method for saccharification of biomass containing cellulose|
US7960325B2|2008-02-15|2011-06-14|Renewable Densified Fuels, Llc|Densified fuel pellets|
US8057639B2|2008-02-28|2011-11-15|Andritz Inc.|System and method for preextraction of hemicellulose through using a continuous prehydrolysis and steam explosion pretreatment process|
US8057666B2|2008-03-11|2011-11-15|Xtrudx Technologies, Inc.|Biomass and waste plastics to neodiesel and valuable chemicals via supercritical water|
US8980143B2|2008-03-11|2015-03-17|Thomas E. Loop|Biomass and waste plastics depolymerization machine and methods via supercritical water|
US7955508B2|2008-03-11|2011-06-07|Xtrudx Technologies, Inc.|Supercritical fluid biomass conversion systems|
ES2643992T3|2008-03-14|2017-11-27|Virginia Tech Intellectual Properties, Inc.|Procedure for pretreatment of lignocellulose using a supercellulose solvent and highly volatile solvents|
RU2371002C1|2008-04-10|2009-10-27|Сергей Моисеевич Бухдрукер|Method of processing plant raw material for fodder|
US8540847B2|2008-05-22|2013-09-24|Aphios Corporation|Methods and apparatus for processing cellulosic biomass|
US20090288788A1|2008-05-22|2009-11-26|Aphios Corporation|Pretreating cellulosic biomass|
US8691722B2|2008-07-03|2014-04-08|Corning Incorporated|Sorbent comprising activated carbon particles, sulfur and metal catalyst|
EP3778717A1|2008-07-16|2021-02-17|Renmatix Inc.|Nano-catalytic-solvo-thermal technology platform bio-refineries|
US8282738B2|2008-07-16|2012-10-09|Renmatix, Inc.|Solvo-thermal fractionation of biomass|
US8119823B2|2008-07-16|2012-02-21|Renmatix, Inc.|Solvo-thermal hydrolysis of xylose|
US8546560B2|2008-07-16|2013-10-01|Renmatix, Inc.|Solvo-thermal hydrolysis of cellulose|
JP5339341B2|2008-08-13|2013-11-13|宜章 大木|Separation method of wood fibers as fiber solids by subcritical state|
KR101070824B1|2008-09-17|2011-10-10|단국대학교 산학협력단|A process and equipment for fractionation and saccharification of biomass|
WO2010034055A1|2008-09-23|2010-04-01|Licella Pty Ltd|Fractionation of lignocellulosic matter|
US8030039B1|2008-10-14|2011-10-04|American Process, Inc.|Method for the production of fermentable sugars and cellulose from lignocellulosic material|
BRPI0919771A2|2008-10-17|2015-08-18|Mascoma Corp|Pure lignin production from cellulosic ligno biomass|
FI121237B|2008-10-21|2010-08-31|Danisco|A process for producing xylose and soluble pulp|
KR101657100B1|2008-10-29|2016-09-19|삼성전자주식회사|Method and Apparatus for Fractionating Lignocellulose-based Biomass|
DE212009000124U1|2008-11-03|2012-02-28|Caidong Qin|Fuel mixture with combustible solid powder and with this fuel mixture operable engine|
CN101736631B|2008-11-12|2011-12-28|熊鹏|Process for efficiently preprocessing lignocellulose|
US8152867B2|2008-12-17|2012-04-10|Bp Biofuels Uk Ltd.|Process, plant and biofuel for integrated biofuel production|
US20110076724A1|2008-12-17|2011-03-31|BP Biofuels UK Limited|Process, Plant, and Biofuel for Integrated Biofuel Production|
US20110126448A1|2008-12-17|2011-06-02|BP Biofuels UK Limited|Process, Plant, and Biofuel For Integrated Biofuel Production|
US20100146842A1|2008-12-17|2010-06-17|Bp Corporation North America Inc.|Process, plant and biofuel for integrated biofuel production|
IT1393929B1|2008-12-18|2012-05-17|Eni Spa|PROCEDURE FOR THE PRODUCTION OF BIO-OIL FROM BIOMASS|
UA117021C2|2008-12-19|2018-06-11|Ксілеко, Інк.|A METHOD FOR THE PROCESSING OF BIOMASS CONTAINING CELLULOSE OR LIGONO-CELLULOUS MATERIALS, A PRODUCT INCLUDING PRE-PROCESSED AND CUTTED AHELLOBEULENOUSLENOUSLUZE|
WO2010081217A1|2009-01-14|2010-07-22|Iogen Energy Corporation|Improved method for the production of glucose from lignocellulosic feedstocks|
WO2010102060A2|2009-03-03|2010-09-10|Poet Research, Inc.|System for pre-treatment of biomass for the production of ethanol|
TW201040279A|2009-03-31|2010-11-16|Chemtex Italia S R L|Improved biomass pretreatment process|
CA2715458C|2009-04-23|2012-05-15|Greenfield Ethanol Inc.|Separation of reactive cellulose from lignocellulosic biomass with high lignin content|
WO2010121367A1|2009-04-23|2010-10-28|Greenfield Ethanol Inc.|Fractionation of biomass for cellulosic ethanol and chemical production|
BRPI1012286A2|2009-05-28|2015-09-22|Lignol Innovations Ltd|native lignin derivatives of annual plant fiber raw materials|
US8378020B1|2009-05-28|2013-02-19|Lignol Innovations Ltd.|Processes for recovery of derivatives of native lignin|
CN101613970B|2009-06-09|2012-10-03|上海士林纤维材料有限公司|Method for preparing bagasse dissolving pulp and pre-extracting hemicellulose and product thereof|
US20100326610A1|2009-06-29|2010-12-30|Harvey J Todd|System and method for continuously treating biomass|
US20120146784A1|2009-06-29|2012-06-14|Robert Winfred Hines|Protective Fabrics and Garments|
CN101586136B|2009-07-03|2012-01-11|中国科学院广州能源研究所|Method of high-efficiency pretreatment on biomass|
US20120138546A1|2009-07-13|2012-06-07|Andrea Bonanni|High Temperature Lignin Separation Process|
CN101613377B|2009-07-21|2012-06-27|清华大学|Biomass supercritical and subcritical combined continuous type pretreatment and hydrolysis equipment and method|
JP2011032388A|2009-08-03|2011-02-17|Nippon Steel Engineering Co Ltd|Fuel production system and method for producing fuel|
US9260464B2|2009-09-25|2016-02-16|Michael A. Lake|Process for recovering lignin|
ES2630053T3|2009-09-29|2017-08-17|Nova Pangaea Technologies Limited|Method and system for fractionation of lignocellulosic biomass|
US8597431B2|2009-10-05|2013-12-03|Andritz Inc.|Biomass pretreatment|
US8383864B2|2009-12-08|2013-02-26|Iowa State University Research Foundation, Inc.|Method for the conversion of cellulose and related carbohydrate materials to low-molecular-weight compounds|
CA2784105A1|2009-12-18|2011-06-23|Shell Internationale Research Maatschappij B.V.|A process for the extraction of sugars and lignin from lignocellulose-comprising solid biomass|
EP3719145A1|2010-01-19|2020-10-07|Renmatix, Inc.|Production of fermentable sugars and lignin from biomass using supercritical fluids|
CN101787398B|2010-01-22|2012-07-25|中国科学院过程工程研究所|Method for purifying, reclaiming and condensing sugar in lignocellulose prehydrolysis liquid|
BR112012019668B1|2010-02-08|2019-04-09|Iogen Energy Corporation|METHOD FOR SCREEN REMOVAL DURING A LIGNOCELLULOSTIC CONVERSION PROCESS|
WO2011099544A1|2010-02-10|2011-08-18|日立化成工業株式会社|Resin composition, molded body and composite molded body|
JP2011219715A|2010-02-10|2011-11-04|Hitachi Chem Co Ltd|Resin compound material for molding|
US20110232160A1|2010-03-25|2011-09-29|Exxonmobil Research And Engineering Company|Biomassconversion process|
US20110253326A1|2010-04-19|2011-10-20|Savannah River Nuclear Solutions, Llc|Separation of Lignin From Lignocellulosic Materials|
CN101886143B|2010-07-13|2012-12-26|大连理工大学|Method for preparing reducing sugar by hydrolyzing biomass with super-critical/sub-critical water in two steps|
WO2012054869A1|2010-10-22|2012-04-26|Bepex International, Llc|System and method for the continuous treatment of solids at non-atmospheric pressure|
PT106039A|2010-12-09|2012-10-26|Hcl Cleantech Ltd|PROCESSES AND SYSTEMS FOR PROCESSING LENHOCELLULOSIC MATERIALS AND RELATED COMPOSITIONS|
KR20120092778A|2011-02-12|2012-08-22|주식회사 팬택|Apparatus and method for performing measurement report considering in-device coexistence interference|
AU2012250572A1|2011-05-04|2013-11-07|Renmatix, Inc.|Multistage cellulose hydrolysis and quench with or without acid|
US8895265B2|2011-05-04|2014-11-25|Renmatix, Inc.|Multistage fractionation process for recalcitrant C5 oligosaccharides|
EP2705045B1|2011-05-04|2016-10-19|Renmatix Inc.|Cellulose hydrolysis with ph adjustment|
WO2012151509A2|2011-05-04|2012-11-08|Renmatix, Inc.|Lignin production from lignocellulosic biomass|
US8801859B2|2011-05-04|2014-08-12|Renmatix, Inc.|Self-cleaning apparatus and method for thick slurry pressure control|
WO2012151526A2|2011-05-04|2012-11-08|Renmatix, Inc.|Enhanced soluble c5 saccharide yields|
WO2012151524A2|2011-05-04|2012-11-08|Renmatix, Inc.|Lignin production from lignocellulosic biomass|
US9518729B2|2011-12-13|2016-12-13|Renmatix, Inc.|Lignin fired supercritical or near critical water generator, system and method|
US8759498B2|2011-12-30|2014-06-24|Renmatix, Inc.|Compositions comprising lignin|
TWI653043B|2012-12-20|2019-03-11|瑞士商伊蘭科動物健康公司|New use|
BR112015023320A2|2013-03-15|2017-07-18|Renmatix Inc|technical lignin; technical lignin having an hsqc nmr spectrum of 1h-13c; and technical lignin which has an nmr spectrum of 13c|WO2012151524A2|2011-05-04|2012-11-08|Renmatix, Inc.|Lignin production from lignocellulosic biomass|
EP2878614A1|2012-05-03|2015-06-03|Virdia Ltd.|Methods for treating lignocellulosic materials|
US20140186627A1|2012-12-28|2014-07-03|Weyerhaeuser Nr Company|Lignin in particulate form|
BR112015023320A2|2013-03-15|2017-07-18|Renmatix Inc|technical lignin; technical lignin having an hsqc nmr spectrum of 1h-13c; and technical lignin which has an nmr spectrum of 13c|
KR20170005418A|2014-05-01|2017-01-13|렌매틱스, 인코포레이티드.|Upgrading lignin from lignin-containing residues through reactive extraction|
DE102014108841B3|2014-06-24|2015-05-28|Technische Universität Hamburg-Harburg|Process for deodorising lignin|
EP3527577A1|2014-07-09|2019-08-21|Virdia, Inc.|Methods for separating and refining lignin from black liquor and compositions thereof|
WO2016049564A1|2014-09-26|2016-03-31|Renmatix, Inc.|Methods for preparing and collecting polyaromatic compounds, and products comprising polyaromatic compounds|
CA2962611A1|2014-09-26|2016-03-31|Renmatix, Inc.|Adhesive compositions comprising type-ii cellulose|
WO2018053530A1|2016-09-19|2018-03-22|Sweetwater Energy, Inc.|Improved foams and films using specialized lignin|
EP3927881A2|2019-02-21|2021-12-29|SunCoal Industries GmbH|Method for reducing the odour in particle-forming carbon materials|
CN112521624A|2019-12-31|2021-03-19|济南圣泉集团股份有限公司|Phenolated lignin, amphoteric lignin emulsifier, emulsified asphalt and preparation method|
WO2022043470A1|2020-08-26|2022-03-03|Suncoal Industries Gmbh|Modified fine particulate carbon materials and method for producing same|
法律状态:
2016-11-03| FGA| Letters patent sealed or granted (standard patent)|
优先权:
申请号 | 申请日 | 专利标题
US201161581865P| true| 2011-12-30|2011-12-30||
US61/581,865||2011-12-30||
US13/472,798|US8759498B2|2011-12-30|2012-05-16|Compositions comprising lignin|
US13/472,798||2012-05-16||
PCT/US2012/067535|WO2013101397A1|2011-12-30|2012-12-03|Compositions comprising lignin|
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