Aso Yuji, Tsubaki Mikikazu, Dang Long Bui Hoang, Murakami Ryo, Nagata Keisuke, Okano Hirohisa, Phuong Dung Ngo Thi, Ohara Hitomi
Department of Biobased Materials Science, Kyoto Institute of Technology, 1 Hashigami-cho, Matsugasaki, Sakyo-ku, Kyoto 606-8585, Japan.
Department of Biobased Materials Science, Kyoto Institute of Technology, 1 Hashigami-cho, Matsugasaki, Sakyo-ku, Kyoto 606-8585, Japan.
J Biosci Bioeng. 2019 Apr;127(4):441-446. doi: 10.1016/j.jbiosc.2018.09.011. Epub 2018 Oct 11.
The present study demonstrates continuous production of d-lactic acid from cellobiose in a cell recycle fermentation with a hollow fiber membrane using recombinant Escherichia coli constructed by deleting its pyruvate formate-lyase activating enzyme gene pflA and expressing a heterologous β-glucosidase on its cell surface. The β-glucosidase gene bglC from Thermobifida fusca YX was cloned into a cell surface display vector pGV3, resulting in pGV3-bglC. Recombinant E. coli JM109 harboring the pGV3-bglC showed β-glucosidase activity (18.9 ± 5.7 U/OD), indicating the cell surface functioning of mutant β-glucosidase. pH-stat cultivation using d-lactic acid producer E. coli BW25113 (ΔpflA) harboring pGV3-bglC in minimum medium with 10 g/L cellobiose in a jar fermentor under anaerobic condition resulted in 5.2 ± 0.1 g/L of d-lactic acid was obtained after 84 h cultivation, indicating that the engineered E. coli produced d-lactic acid directly from cellobiose. For continuous d-lactic acid production, cell recycle fermentation was conducted under anaerobic condition and the culture was continuously ultrafiltrated with a hollow fiber cartridge. The permeate was drawn to the reservoir and a minimum medium containing 10 g/L cellobiose was fed to the fermentor at the same rate (dilution rate, 0.05 h). Thus, this system maintained the d-lactic acid production (4.3-5.0 g/L), d-lactic acid production rate (0.22-0.25 g/L/h), and showed no residual cellobiose in the culture during 72 h operation. Interestingly, the d-lactic acid production rate in cell recycle fermentation was more than 3 times higher than that in the batch operation (0.06 ± 0.00 g/L/h).
本研究表明,在细胞循环发酵中,使用通过缺失其丙酮酸甲酸裂解酶激活酶基因pflA构建并在其细胞表面表达异源β-葡萄糖苷酶的重组大肠杆菌,可从纤维二糖连续生产d-乳酸。将来自嗜热栖热放线菌YX的β-葡萄糖苷酶基因bglC克隆到细胞表面展示载体pGV3中,得到pGV3-bglC。携带pGV3-bglC的重组大肠杆菌JM109表现出β-葡萄糖苷酶活性(18.9±5.7 U/OD),表明突变型β-葡萄糖苷酶在细胞表面发挥功能。在厌氧条件下,使用携带pGV3-bglC的d-乳酸生产菌大肠杆菌BW25113(ΔpflA)在装有10 g/L纤维二糖的基本培养基中于罐式发酵罐中进行pH-stat培养,培养84小时后得到5.2±0.1 g/L的d-乳酸,这表明工程化的大肠杆菌可直接从纤维二糖生产d-乳酸。为了连续生产d-乳酸,在厌氧条件下进行细胞循环发酵,并使用中空纤维柱对培养物进行连续超滤。将渗透液引入储液器,并以相同速率(稀释率为0.05 h)将含有10 g/L纤维二糖的基本培养基加入发酵罐。因此,该系统在72小时的运行过程中保持了d-乳酸的产量(4.3 - 5.0 g/L)、d-乳酸生产率(0.22 - 0.25 g/L/h),并且培养物中没有残留纤维二糖。有趣的是,细胞循环发酵中的d-乳酸生产率比分批操作中的生产率(0.06±0.0 g/L/h)高出3倍以上。