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Evaluation of an electrochemical bioreactor system in the biotransformation of 6-bromo-2-tetralone to 6-bromo-2-tetralol

机译:在6-溴-2-四氢萘酮向6-溴-2-四氢萘酚生物转化中电化学生物反应器系统的评估

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摘要

Biotransformation of 6-bromo-2-tetralone (Br-β-tetralone) to 6-bromo-2-tetralol (Br-β-tetralol) by yeast cells of Trichosporon capitatum (ATCC 74312) and its partially purified Br-β-tetralone reductase was evaluated in an electrochemical bioreactor. The biotransformation rates and final product formation were significantly affected by substrate concentration, biomass and electric potential. At 2 g/l of substrate, the initial reaction rate and final product were increased by 35% and 15%, respectively, with –1.5 V of electric potential compared to without electric potential. Additional substrate (2 g/l) provided by pulse feeding to the reaction mixture at different intervals resulted in 2.1 g/l Br-β-tetralol compared to a total of 1.2 g/l without feeding. However, the increased production was not proportionate to the amount of additionally fed substrate. Increased substrate availability by the addition of 5% (v/v) ethanol resulted in the highest reaction rate and product formation, but addition of ethanol at a concentration higher than 5% decreased the reaction rate. At low biomass, the initial reaction rates were enhanced significantly when electric potential was high, but a higher biomass was necessary to obtain a similar reaction rate when electric potential was reduced. The highest initial reaction rate (59.2 mg/l per min) was achieved with a two-fold biomass concentration of 15.6 g of dry cell weight/l, substrate at 4 g/l and electric potential at –6 V. The conversion of Br-β-tetralone to Br-β-tetralol with partially purified Br-β-tetralone reductase was slow in the presence of electric potential.
机译:头孢霉菌(Trichosporon capitatum)(ATCC 74312)的酵母细胞及其部分纯化的Br-β-四氢萘酮将6-溴-2-四氢萘酮(Br-β-四氢萘酮)生物转化为6-溴-2-四氢萘酚(Br-β-四氢萘酚)在电化学生物反应器中评估还原酶。生物转化率和最终产物形成受底物浓度,生物量和电势显着影响。与没有电势时相比,在2 g / l的底物下,电势为–1.5 V时,初始反应速率和最终产物分别增加了35%和15%。通过以不同间隔脉冲进料到反应混合物中提供的额外底物(2 g / l)产生2.1 g / lBr-β-四醇,而没有进料的总量为1.2 g / l。然而,增加的产量与额外进料的基材的量不成比例。通过添加5%(v / v)乙醇可增加底物的利用率,从而导致最高的反应速率和产物形成,但是添加浓度高于5%的乙醇会降低反应速率。在低生物量下,当电势高时,初始反应速率显着提高,但是当电势降低时,需要更高的生物量才能获得相似的反应速率。最高的初始反应速率(每分钟59.2 mg / l)是生物量浓度的两倍,即干细胞重量为15.6 g / l,底物为4 g / l,电势为–6V。Br的转化在存在电势的情况下,用部分纯化的Br-β-四氢萘酮还原酶将-β-四氢萘酮转化为Br-β-四氢呋喃的速度很慢。

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  • 来源
    《Applied Microbiology and Biotechnology》 |2001年第4期|506-510|共5页
  • 作者单位

    MBI International P.O. Box 27609 Lansing MI 48909 USA;

    MBI International P.O. Box 27609 Lansing MI 48909 USA;

    Bioprocess Research and Development Merck Research Laboratories P.O. Box 2000 Rahway NJ 07065-0900 USA;

    MBI International P.O. Box 27609 Lansing MI 48909 USA;

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