首页> 外国专利> Process for obtaining active L--amino carboxylic acids from corresponding racemic d, L--amino carboxylic acids

Process for obtaining active L--amino carboxylic acids from corresponding racemic d, L--amino carboxylic acids

机译:从相应的外消旋d,L-氨基羧酸获得活性L-氨基羧酸的方法

摘要

The disclosure relates to a process for obtaining optically active L-. alpha.-aminocarboxylic acids from the corresponding racemic D, L,. alpha.- aminocarboxylic acids. The following steps are involved: (a) the D,L,. alpha.-aminocarboxylic acids are acetylated; (b) the N-acetyl-L- . alpha.- aminocarboxylic acid present in the mixture of N-acetyl-D,L,. alpha.- aminocarboxylic acids thus obtained is broken down enzymatically into the L--aminocarboxylic acid; (c) the L-- aminocarboxylic acid is separated from the mixture, a quantity of a solution of N-acetyl- D(L)-. alpha.-aminocarboxylic acids and a quantity of acetate equivalent to the L--aminocarboxylic acid being retained; and (d) the N-acetyl- D(L)-. alpha.-aminocarboxylic acid is racemized and recycled for enzymatic breakdown. Known extraction processes involving steps (a) to (d) have the disadvantage of producing large quantities of salt. Specifically, the processes are far removed from the ideal equation, according to which one hundred percent of the acetic anhydride and the D, L,- aminocarboxylic acids are converted to L--aminocarboxylic acids and acetic acid. Adjusting the retained solution from step (c) in such a way as to obtain a solution consisting essentially of N-acetyl-D- (L)-. alpha.-aminocarboxylic acid salt and free acetic acid in equilibrium with acetate and free N-acetyl- D(L)--aminocarboxylic acid and from which acetic acid is extracted by distillation makes it surprisingly easy to feed the solution formed as "mother liquor" following separation of the L-- aminocarboxylic acid in the circuit and to achieve a materials balance as close as possible to the ideal.
机译:本公开涉及一种用于获得旋光L-的方法。来自相应外消旋体D,L的α-氨基羧酸。 α.-氨基羧酸。涉及以下步骤:(a)D,L ,。 α.-氨基羧酸被乙酰化; (b)N-乙酰基-L-。在N-乙酰基-D,L 1的混合物中存在α-氨基羧酸。如此获得的α.-氨基羧酸被酶分解为L-氨基羧酸; (c)从混合物中分离出L-氨基羧酸,N-乙酰基-D(L)-溶液的量。保留了α-氨基羧酸和相当于L-氨基羧酸的乙酸盐数量; (d)N-乙酰基-D(L)-。外消旋α-氨基羧酸并循环用于酶促分解。涉及步骤(a)至(d)的已知提取方法具有产生大量盐的缺点。具体而言,该方法与理想方程式相去甚远,根据该方程式,乙酸酐和D,L,-氨基羧酸的百分率被转化为L-氨基羧酸和乙酸。调节步骤(c)中保留的溶液,以得到基本上由N-乙酰基-D-(L)-组成的溶液。 α.-氨基羧酸盐和游离乙酸与乙酸盐和游离N-乙酰基-D(L)-氨基羧酸平衡,并且通过蒸馏从中提取乙酸,这使得加入“母液”形成的溶液非常容易然后在回路中分离L-氨基羧酸并达到尽可能接近理想的材料平衡。

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