含苯丙氨酸解氨酶的粘红酵母细胞反式肉桂酸转化为l -苯丙氨酸过程中反应条件优化及稳定性研究。

Acta microbiologica Polonica Pub Date : 2002-01-01
Ahmed I El-Batal
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引用次数: 0

摘要

研究了含粘红酵母细胞的l -苯丙氨酸解氨酶(PAL)将反式肉桂酸(t-CA)生物转化为l -苯丙氨酸(l -苯丙氨酸)的最佳反应条件(pH、温度、氨浓度和生物催化剂负载)。除Triton X-100外,所有使用渗透剂的处理都刺激了l -苯丙氨酸的产生,也增强了催化剂的不稳定性,与对照相比,Triton X-100的转化率提高了56%,PAL酶也得到了显著的稳定。在生物转化过程中,在反应混合物中加入几种活性改性剂和稳定剂添加剂,可以提高l -苯丙氨酸的产量,并在几次连续孵育中保持苯丙氨酸的稳定性。加入20%的多羟基醇(甘油)可以最大限度地稳定PAL和提高l -苯丙氨酸的产量。在重复间歇过程中,l -苯丙氨酸的生产持续到第5个循环,总产量比对照(不添加甘油)提高了2.3倍。为了降低氧对PAL催化剂寿命的影响,在生物转化混合物中加入了2-巯基乙醇和巯基乙酸等还原剂。添加400 mg(-1)巯基乙酸的l -苯丙氨酸产量比对照提高了55%。当20%甘油和400 mg(-1)巯基乙酸同时存在于反应混合物中时,生物催化剂(PAL)的可重复使用性和稳定性延长至连续8个循环,l -苯丙氨酸的转化率和总生产率均高于对照组。这些结果可能导致必需氨基酸l -苯丙氨酸生产的改善。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Optimization of reaction conditions and stabilization of phenylalanine ammonia lyase-containing Rhodotorula glutinis cells during bioconversion of trans-cinnamic acid to L-phenylalanine.

Studies were performed to elucidate the optimal reaction conditions (pH, temperature, ammonia concentration and biocatalyst loading) for bioconversion of trans-cinnamic acid (t-CA) to L-phenylalanine (L-Phe) by L-phenylalanine ammonia lyase (PAL) containing Rhodotorula glutinis cells. All treatments with permeabilizing agents stimulated L-Phe production and also enhanced instability of the catalyst, except Triton X-100 which gave a superior (56%) increase in conversion as compared to the control and a significant stabilization of PAL enzyme. Inclusion of several activity modifiers and stabilizer additives in reaction mixtures were shown to enhance the yield of L-Phe and maintained PAL stability over several successive incubations during the bioconversion process. Maximum stabilization of PAL and enhancement of L-Phe production was achieved with addition of 20% polyhydric alcohol (glycerol). The production of L-Phe continued to the fifth cycle and the total yield increased 2.3 times compared to the yield produced by the control (without glycerol addition) during the repeated batch process. Reducing agents such as 2-mercaptoethanol and thioglycolic acid were added to the bioconversion mixture in order to reduce the effects of oxygen on PAL catalyst life. Production of L-Phe by addition of 400 mgL(-1) of thioglycolic acid was maximized over the control by 55%. When both 20% glycerol and 400 mgL(-1) thioglycolic acid were simultaneously present in the reaction mixture, reuseability and stability of biocatalyst (PAL) were extended to eight consecutive cycles and conversion rate and overall productivity of L-Phe were higher than that of the control. These results may lead to improvements in the production of the essential amino acid L-Phe.

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