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    • 1. 发明授权
    • Recovery of fermentation salts from dilute aqueous solutions
    • 从稀水溶液中回收发酵盐
    • US06478965B1
    • 2002-11-12
    • US09441211
    • 1999-11-16
    • Mark T. HoltzappleRichard R. DavisonTorsten Luettich
    • Mark T. HoltzappleRichard R. DavisonTorsten Luettich
    • B01D1102
    • B01D17/042B01D11/0457B01D17/00B01D17/0211B01D17/0214B01D17/041B01D17/044B01D17/045B01D17/047B01D17/048C07C51/48C07C53/08
    • Dilute solutions of fermentation sales may be concentrated by extracting water using low-miscibility, low-molecular-weight secondary and tertiary amines, e.g. triethylamine (TEA), diisopropyl amine (DIA), N,N-diethylmethylamine (DEMA), and mixtures thereof. At 30° C.-55° C., which corresponds to typical fermentation temperatures, these low-molecular-weight amines or their mixtures, can extract large amounts of water from dilute aqueous solutions containing fermentation salts. Thus, dilute fermentation salt solutions can be concentrated by selectively removing water. At these low temperatures, the amine phase contains 20-35% water and a much reduced quantity of fermentation salt. When the temperature is raised, water phases out of the amine, allowing the amine to be recycled and reused to extract additional water. Using this approach, about 82.5% of water can be removed from a 3% dilute solution using conventional multistage, countercurrent extraction, thus providing a 15% concentrated fermentation salt solution.
    • 发酵销售的稀释溶液可以通过使用低混溶性,低分子量仲胺和叔胺例如水, 三乙胺(TEA),二异丙胺(DIA),N,N-二乙基甲胺(DEMA)及其混合物。 这些低分子量胺或其混合物在30℃-55℃下对应于典型的发酵温度,可以从含有发酵盐的稀释水溶液中提取大量的水。 因此,可以通过选择性除去水来浓缩稀释的发酵盐溶液。 在这些低温下,胺相含有20-35%的水和大量减少的发酵盐。 当温度升高时,水从胺中脱出,允许胺再循环并重新使用以提取额外的水。 使用这种方法,可以使用常规的多级逆流提取,从3%稀释溶液中除去约82.5%的水,从而提供15%浓缩的发酵盐溶液。
    • 2. 发明授权
    • Recovery of fermentation salts from dilute aqueous solutions
    • 从稀水溶液中回收发酵盐
    • US5986133A
    • 1999-11-16
    • US885841
    • 1997-06-30
    • Mark T. HoltzappleRichard R. DavisonTorsten Luettich
    • Mark T. HoltzappleRichard R. DavisonTorsten Luettich
    • C12P7/54B01D11/04B01D17/00B01D17/04C07C51/48C07C53/08C07C55/10C07C59/08C12P7/40C07C51/42
    • B01D17/042B01D11/0457B01D17/00B01D17/041C07C51/48
    • Dilute solutions of fermentation sales may be concentrated by extracting water using low-miscibility, low-molecular-weight secondary and tertiary amines, e.g. triethylamine (TEA), diisopropyl amine (DIA), N,N-diethylmethylamine (DEMA), and mixtures thereof. At 30.degree. C.-55.degree. C., which corresponds to typical fermentation temperatures, these low-molecular-weight amines or their mixtures, can extract large amounts of water from dilute aqueous solutions containing fermentation salts. Thus, dilute fermentation salt solutions can be concentrated by selectively removing water. At these low temperatures, the amine phase contains 20-35% water and a much reduced quantity of fermentation salt. When the temperature is raised, water phases out of the amine, allowing the amine to be recycled and reused to extract additional water. Using this approach, about 82.5% of water can be removed from a 3% dilute solution using conventional multistage, countercurrent extraction, thus providing a 15% concentrated fermentation salt solution.
    • 发酵销售的稀释溶液可以通过使用低混溶性,低分子量仲胺和叔胺例如水, 三乙胺(TEA),二异丙胺(DIA),N,N-二乙基甲胺(DEMA)及其混合物。 这些低分子量胺或其混合物在30℃-55℃下对应于典型的发酵温度,可以从含有发酵盐的稀释水溶液中提取大量的水。 因此,可以通过选择性除去水来浓缩稀释的发酵盐溶液。 在这些低温下,胺相含有20-35%的水和大量减少的发酵盐。 当温度升高时,水从胺中脱出,允许胺再循环并重新使用以提取额外的水。 使用这种方法,可以使用常规的多级逆流提取,从3%稀释溶液中除去约82.5%的水,从而提供15%浓缩的发酵盐溶液。
    • 3. 发明申请
    • SYSTEM AND METHOD FOR CONVERTING BIOMASS
    • 用于转化生物量的系统和方法
    • US20100152485A1
    • 2010-06-17
    • US12699669
    • 2010-02-03
    • Mark T. HoltzappleRichard R. DavisonCesar B. GrandaFrank K. AgbogboZhihong Fu
    • Mark T. HoltzappleRichard R. DavisonCesar B. GrandaFrank K. AgbogboZhihong Fu
    • C07C61/00C07C35/00
    • C12P7/02C12P7/40Y02E50/16
    • In accordance with the teachings of the present invention, a system and method converting biomass into useful chemicals are provided. In a particular embodiment, the method includes fermenting biomass in one or more fermentors to produce a fermentation broth comprising ammonium carboxylate salts, the fermentors containing an ammonium carbonate or ammonium bicarbonate buffer. The method further includes reacting the ammonium carboxylate salts from the fermentors with a high-molecular-weight amine to produce amine carboxylate salt, and thermally cracking the amine carboxylate salt to produce carboxylic acid. In another embodiment, the ammonium carboxylate salts from the fermentors may be reacted with a low-molecular-weight amine to produce a low-molecular-weight-amine carboxylate salt. The low-molecular-weight amine in the low-molecular-weight-amine carboxylate salt may then be switched with a high-molecular-weight amine to form a high-molecular-weight-amine carboxylate salt, which is then thermally cracked to produce carboxylic acid.
    • 根据本发明的教导,提供了将生物质转化为有用化学物质的系统和方法。 在一个具体实施方案中,该方法包括在一个或多个发酵罐中发酵生物质以产生包含羧酸铵盐的发酵液,所述发酵罐含有碳酸铵或碳酸氢铵缓冲液。 该方法还包括使来自发酵罐的羧酸铵盐与高分子量胺反应以产生胺羧酸盐,并热分解胺羧酸盐以产生羧酸。 在另一个实施方案中,来自发酵罐的羧酸铵盐可以与低分子量胺反应以产生低分子量 - 羧酸盐。 然后可以用高分子量胺转化低分子量羧酸盐中的低分子量胺形成高分子量胺羧酸盐,然后将其热裂解产生 羧酸。
    • 6. 发明授权
    • Calcium hydroxide pretreatment of biomass
    • 生物质氢氧化钙预处理
    • US5693296A
    • 1997-12-02
    • US300543
    • 1994-09-06
    • Mark T. HoltzappleRichard R. DavisonMurlidhar Nagwani
    • Mark T. HoltzappleRichard R. DavisonMurlidhar Nagwani
    • A23K10/32C01F11/18C12P7/10C13K1/02C01F11/02A23K1/12C01F11/06
    • C12P7/10A23K10/32C01F11/18C13K1/02Y02E50/16
    • Lignocellulose-containing materials are treated with lime (calcium hydroxide) and water at a relatively high temperature and for a certain period of time under certain conditions. The process variables were: lime loading which ranged from about 2 to about g Ca(OH).sub.2 /100 g dry material; water loading which ranged from about 6 to about 19 g water/g dry material; treatment temperature which varied from about 50.degree. C. to about 150.degree. C.; and treatment time which varied from about 1 to about 36 hours. The effects of treatment time and temperature were interdependent. A process for lime recovery is developed. The soluble Ca(OH).sub.2 was washed out of the pretreated material with water and converted to insoluble CaCO.sub.3, by reacting with CO.sub.2, and was thus separated. The CaCO.sub.3 can be heated to produce CaO and CO.sub.2. The CaO is hydrated to Ca(OH).sub.2 which can be reused as the lignocellulose treatment agent. Carbon dioxide is reused for lime recovery.
    • 含木质纤维素的材料在比较高的温度下用石灰(氢氧化钙)和水处理并在一定条件下处理一段时间。 过程变量为:约2至约g Ca(OH)2 / 100g干物料的石灰负荷; 水含量范围为约6至约19克水/克干物质; 处理温度从约50℃变化到约150℃。 治疗时间约1〜36小时。 治疗时间和温度的影响是相互依存的。 开发了石灰回收方法。 将可溶性Ca(OH)2用水从预处理物质中洗出,并与CO 2反应转化为不溶性CaCO 3,由此分离。 可以加热CaCO3以产生CaO和CO 2。 CaO与Ca(OH)2水合,可以作为木质纤维素处理剂再次使用。 二氧化碳重新用于石灰回收。