首页> 外国专利> PROCEDURES FOR THE RECEIVING OF OPTICAL ACTIVE L-ALPHA-AMINOCARBONIC ACIDS FROM RECEIVING RACEMIC D,L-ALPHA-AMINOCARBONIC ACIDS

PROCEDURES FOR THE RECEIVING OF OPTICAL ACTIVE L-ALPHA-AMINOCARBONIC ACIDS FROM RECEIVING RACEMIC D,L-ALPHA-AMINOCARBONIC ACIDS

机译:从RACEMIC D,L-α-氨基碳酸盐中接收光学活性L-α-氨基碳酸盐的方法

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- alpha -aminocarboxylic acid; (c) the L- alpha -aminocarboxylic acid is separated from the mixture, a quantity of a solution with N-acetyl-D(L)- alpha -aminocarboxylic acids and a quantity of acetate equivalent to the L- alpha -aminocarboxylic acid being retained; and (d) the N-acetyl-D(L)- alpha -aminocarboxylic acid is racemised and recycled for enzymatic breakdown. Known extraction processes involving steps (a) to (d) have the disadvantage of producing large quantities of salts. Specifically, the processes are far removed from the ideal equation, according to which one hundred percent of the acetic anhydride and the D,L, alpha -aminocarboxylic acids are converted to L- alpha -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)- alpha -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- alpha -aminocarboxylic acids in the circuit and to achieve a materials balance as close as possible to the ideal.
机译:本公开涉及从相应的外消旋D,L,α-氨基羧酸获得旋光的L-α-氨基羧酸的方法。涉及以下步骤:(a)将D,L,α-氨基羧酸乙酰化; (b)将如此获得的N-乙酰基-D,L,α-氨基羧酸的混合物中存在的N-乙酰基-L-α-氨基羧酸酶分解为L-α-氨基羧酸; (c)从混合物中分离出L-α-氨基羧酸,一定量的具有N-乙酰基-D(L)-α-氨基羧酸的溶液和一定量的等于L-α-氨基羧酸的乙酸盐为保留(d)将N-乙酰基-D(L)-α-氨基羧酸消旋并再循环用于酶促分解。涉及步骤(a)至(d)的已知提取方法具有产生大量盐的缺点。具体地,该方法与理想方程式相去甚远,根据该理想方程式,乙酸酐和D,L,α-氨基羧酸的百分之一百被转化为L-α-氨基羧酸和乙酸。调整步骤(c)中的保留溶液,以使溶液基本上由N-乙酰基-D-(L)-α-氨基羧酸盐和游离乙酸组成,并与乙酸盐和游离N-乙酰基-酯平衡D(L)-α-氨基羧酸,通过蒸馏从中萃取出乙酸,使得在回路中分离L-α-氨基羧酸之后,很容易将形成为“母液”的溶液进料,并获得了一种材料尽可能接近理想的平衡。

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