Department of Biotechnology, Himachal Pradesh University, Summer Hill, Shimla, 171005, India.
AMB Express. 2012 Apr 26;2(1):25. doi: 10.1186/2191-0855-2-25.
Isonicotinic acid (INA) is an important pyridine derivative used in the manufacture of isoniazid (antituberculosatic drug) and other pharmaceutically important drugs. Nitrilase catalysed processes for the synthesis of pharmaceutically important acids from their corresponding nitriles are promising alternative over the cumbersome, hazardous, and energy demanding chemical processes. Nitrilase of Nocardia globerula NHB-2 (NitNHB2) is expressed in presence of isobutyronitrile in the growth medium (1.0% glucose, 0.5% peptone, 0.3% beef extract, and 0.1 % yeast extract, pH 7.5). NitNHB2 hydrolyses 4-cyanopyridine (4-CP) to INA without accumulation of isonicotinamide, which is common in the reaction catalysed via fungal nitrilases. The NitNHB2 suffers from substrate inhibition effect and hydrolysing activity up to 250 mM 4-CP was recorded. Complete conversion of 200 mM 4-CP to INA was achieved in 40 min using resting cell concentration corresponding to 10 U mL-1 nitrilase activity in the reaction. Substrate inhibition effect in the fed batch reaction (200 mM substrate feed/40min) led to formation of only 729 mM INA. In a fed batch reaction (100 mM 4-CP/20min), substrate inhibition effect was encountered after 7th feed and a total of 958 mM INA was produced in 400 min. The fed batch reaction scaled up to 1 L and 100% hydrolysis of 700 mM of 4-CP to INA at 35°C achieved in 140 min. The rate of INA production was 21.1 g h-1 mgDCW-1. This is the fastest biotransformation process ever reported for INA production with time and space productivity of 36 g L-1 h-1 using a bacterial nitrilase.
异烟酸(INA)是一种重要的吡啶衍生物,用于制造异烟肼(抗结核药物)和其他重要的药物。与繁琐、危险和能源密集型的化学工艺相比,腈水解酶催化的从相应腈合成重要药物的方法是很有前途的替代方法。在生长培养基(1.0%葡萄糖、0.5%蛋白胨、0.3%牛肉提取物和 0.1%酵母提取物,pH7.5)中,诺卡氏菌 globerula NHB-2(NitNHB2)的表达伴随着异丁腈的存在。NitNHB2 水解 4-氰基吡啶(4-CP)生成 INA,而不积累常见于真菌腈水解酶催化反应中的烟酰胺。NitNHB2 受到底物抑制效应的影响,在 250 mM 4-CP 下记录到水解活性。用对应于 10 U mL-1 酶活的静止细胞浓度,在 40 min 内完成了 200 mM 4-CP 到 INA 的完全转化。在分批补料反应(200 mM 底物进料/40 min)中,底物抑制效应导致仅形成 729 mM INA。在分批补料反应(100 mM 4-CP/20 min)中,在第 7 次进料后遇到了底物抑制效应,在 400 min 内总共产生了 958 mM INA。分批补料反应扩大到 1 L,在 35°C 下,700 mM 4-CP 100%水解,在 140 min 内实现 INA 的生成。INA 的生成速率为 21.1 g h-1 mgDCW-1。这是使用细菌腈水解酶生产 INA 的最快生物转化过程,时间和空间生产率分别为 36 g L-1 h-1。