Lee D C, Kim H S
Department of Biological Sciences, Korea Advanced Institute of Science and Technology, 373-1, Kusung-Dong, Yusung-Gu, Taejon 305-701, Korea.
Biotechnol Bioeng. 1998 Dec 20;60(6):729-38. doi: 10.1002/(sici)1097-0290(19981220)60:6<729::aid-bit9>3.0.co;2-g.
A thermostable D-hydantoinase from Bacillus stearothermophilus SD-1 was previously mass-produced by batch cultivation of the recombinant E. coli harboring the gene encoding the enzyme (Lee et al., 1997). In this work, we attempted to optimize the process for the production of N-carbamoyl-D-p-hydroxyphenylglycine, which is readily hydrolyzed to D-p-hydroxyphenylglycine under acidic conditions, from 5-(4-hydroxyphenyl)hydantoin using the mass-produced D-hydantoinase. In an effort to overcome the low solubility of the substrate, enzyme reaction was carried out in a heterogeneous system consisting of a high substrate concentration up to 300 g/L. In this reaction system, most of substrate is present in suspended particles. Optimal temperature and pH were determined to be 45 degrees C and 8.5, respectively, by taking into account the reaction rate and conversion yield. When the free enzyme was employed as a biocatalyst, enzyme loading higher than 300 unit/g-substrate was required to achieve maximum conversion. Use of whole cell enzyme resulted in maximum conversion even at lower enzyme loadings than the free enzyme, showing 96% conversion yield at 300 g/L substrate. The heterogeneous reaction system used in this work might be applied to the enzymatic production of other valuable compounds from a rarely water-soluble substrate.
嗜热脂肪芽孢杆菌SD-1的一种耐热D-海因酶先前通过对携带该酶编码基因的重组大肠杆菌进行分批培养实现了大规模生产(Lee等人,1997年)。在这项工作中,我们尝试优化使用大规模生产的D-海因酶从5-(4-羟基苯基)海因生产N-氨甲酰-D-对羟基苯甘氨酸的工艺,该物质在酸性条件下可容易地水解为D-对羟基苯甘氨酸。为了克服底物的低溶解度,酶反应在由高达300 g/L的高底物浓度组成的非均相体系中进行。在该反应体系中,大部分底物以悬浮颗粒形式存在。通过考虑反应速率和转化率,确定最佳温度和pH分别为45℃和8.5。当使用游离酶作为生物催化剂时,需要高于300单位/克底物的酶负载量才能实现最大转化率。使用全细胞酶即使在比游离酶更低的酶负载量下也能实现最大转化率,在300 g/L底物时显示出96%的转化率。这项工作中使用的非均相反应体系可能适用于从难溶于水的底物酶促生产其他有价值的化合物。