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    • 5. 发明授权
    • Process for the recovery of organic acids from aqueous solutions
    • 从水溶液中回收有机酸的方法
    • US06670505B1
    • 2003-12-30
    • US09519936
    • 2000-03-07
    • Nick Allen CollinsMark Robert SheltonGeorge William TindallSteven Thomas PerriRuairi Seosamh O'MeadhraChester Wayne SinkBhaskar Krishna ArumugamJohn Clark Hubbs
    • Nick Allen CollinsMark Robert SheltonGeorge William TindallSteven Thomas PerriRuairi Seosamh O'MeadhraChester Wayne SinkBhaskar Krishna ArumugamJohn Clark Hubbs
    • C07C5142
    • C07C51/43Y02P20/582Y10S435/803Y10S435/876Y10S435/896C07C59/347
    • A process for recovering a desired organic acid from a solution includes the steps of: providing an aqueous solution including at least one desired organic acid or its acid anion; adjusting the proton concentration in the aqueous solution to a desired level, with the desired proton concentration being selected, at least in part, by the amount of available protons needed to associate with the acid anions of the desired organic acid(s) to be recovered and/or acid anions that are weaker than the desired organic acids; and recovering at least a portion of the at least one desired organic acid from the aqueous phase. The desired proton concentration can be based on the amount of available protons being greater than, less than or substantially equal, to the amount of protons needed to associate with the anion of the desired organic acid(s) and acid anions that are weaker than the desired organic acid(s). Specific examples of suitable organic acids include, but are not limited to, ascorbic, succinic, tartaric, glyconic, gulonic, citric, lactic, hialic, maleic, acetic, formic, gluconic pyruvic, propionic, butyric, itaconic acids and mixtures thereof. One embodiment of the present invention relates to the recovery of 2-keto-L-gulonic acid (KLG) from aqueous solutions such as fermentation baths.
    • 从溶液中回收所需有机酸的方法包括以下步骤:提供包含至少一种所需有机酸或其酸阴离子的水溶液; 将所述水溶液中的质子浓度调节到所需的水平,其中所需质子浓度至少部分地被选择与需要回收的所需有机酸的酸性阴离子缔合所需的可用质子的量 和/或弱于所需有机酸的酸性阴离子; 以及从所述水相中回收所述至少一种所需有机酸的至少一部分。 期望的质子浓度可以基于可用质子的量大于,小于或基本上等于与所需有机酸的阴离子和酸阴离子相比所需的质子的量,其弱于 合适的有机酸的具体实例包括但不限于抗坏血酸,琥珀酸,酒石酸,葡萄糖酸,古洛糖酸,柠檬酸,乳酸,唾液酸,马来酸,乙酸,甲酸,葡萄糖酸,丙酸,丙酸,丁酸, 衣康酸及其混合物。 本发明的一个实施方案涉及从水溶液如发酵浴中回收2-酮-L-古洛糖酸(KLG)。
    • 7. 发明授权
    • Process for the preparation of ascorbic acid
    • 抗坏血酸的制备方法
    • US06476239B1
    • 2002-11-05
    • US10074829
    • 2002-02-12
    • Bhaskar Krishna ArumugamSteven Thomas PerriElaine Beatrice MackenzieLarry Wayne BlairJoseph Robert Zoeller
    • Bhaskar Krishna ArumugamSteven Thomas PerriElaine Beatrice MackenzieLarry Wayne BlairJoseph Robert Zoeller
    • C07D30762
    • C07D307/62
    • The present invention is a process for the preparation of ascorbic acid using a simulated moving bed (SMB) reactor system to accomplish the simultaneous conversion of KLG or a derivative of KLG to ascorbic acid and the separation of reaction products. The SMB reactor contains a solid or mixture of solids effective for catalyzing the reaction of KLG or its derivative and for separating the reactions products by selective adsorption of at least one product. In a general embodiment, this process involves (1) feeding a solution of KLG or a derivative thereof in a first solvent and a desorbent which is miscible with the first solvent, to a simulated moving bed reactor; (2) reacting the KLG or the KLG derivative to form ascorbic acid; and (3) removing from the simulated moving bed reactor (i) a first liquid stream comprising a solution of ascorbic acid in the desorbent and the first solvent (ii) a second liquid stream comprising the first solvent and the desorbent.
    • 本发明是使用模拟移动床(SMB)反应器系统制备抗坏血酸的方法,以实现KLG或KLG的衍生物同时转化为抗坏血酸和分离反应产物。 SMB反应器含有对催化KLG或其衍生物的反应有效的固体或固体混合物,并且通过选择性吸附至少一种产物来分离反应产物。 在一般实施方案中,该方法包括(1)将KLG或其衍生物的溶液送入模拟移动床反应器中的第一溶剂和可与第一溶剂混溶的解吸剂; (2)使KLG或KLG衍生物反应形成抗坏血酸; (3)从模拟移动床反应器(i)中除去包含解吸剂中的抗坏血酸溶液的第一液体流和第一溶剂(ii)包含第一溶剂和解吸剂的第二液体流。