Santolin Lara, Waldburger Saskia, Neubauer Peter, Riedel Sebastian L
Chair of Bioprocess Engineering, Institute of Biotechnology, Technische Universität Berlin, Berlin, Germany.
Front Bioeng Biotechnol. 2021 Mar 22;9:623890. doi: 10.3389/fbioe.2021.623890. eCollection 2021.
Recent studies of the impact and dimension of plastic pollution have drawn the attention to finding more sustainable alternatives to fossil-based plastics. Microbially produced polyhydroxyalkanoates (PHAs) biopolymers are strong candidates to replace conventional plastic materials, due to their true biodegradability and versatile properties. However, widespread use of these polymers is still hindered by their high cost of production. In the present study, we target high yields of the PHA copolymer poly(hydroxybutyrate--hydroxyhexanoate) [P(HB--HHx)] using a substrate-flexible two-stage fed-batch approach for the cultivation of the recombinant strain Re2058/pCB113. A more substrate-flexible process allows to cope with constant price fluctuations and discontinuous supply of feedstocks on the market. Utilizing fructose for biomass accumulation and rapeseed oil for polymer production resulted in a final biomass concentration of 124 g L with a polymer content of 86 wt% holding 17 mol% of HHx. Productivities were further optimized by operating the biomass accumulation stage in a "drain and fill" modus where 10% of the culture broth was recycled for semi-continuous biomass accumulation, after transferring 90% to a second bioreactor for PHA production. This strategy succeeded in shortening process times rising productivity yields to ∼1.45 g L h.
近期关于塑料污染影响和规模的研究促使人们关注寻找更可持续的化石基塑料替代品。微生物产生的聚羟基脂肪酸酯(PHA)生物聚合物是替代传统塑料材料的有力候选者,因为它们具有真正的生物可降解性和多样的性能。然而,这些聚合物的广泛应用仍受到其高生产成本的阻碍。在本研究中,我们使用底物灵活的两阶段补料分批培养法培养重组菌株Re2058/pCB113,以实现PHA共聚物聚(3-羟基丁酸酯-3-羟基己酸酯)[P(HB-HHx)]的高产率。更具底物灵活性的工艺能够应对市场上原料价格的持续波动和供应的不连续性。利用果糖进行生物质积累,菜籽油进行聚合物生产,最终生物质浓度达到124 g/L,聚合物含量为86 wt%,其中HHx含量为17 mol%。通过在“排出并补充”模式下操作生物质积累阶段进一步优化了生产率,即在将90%的培养液转移到第二个生物反应器进行PHA生产后,将10%的培养液循环用于半连续生物质积累。该策略成功缩短了工艺时间,使生产率提高到约1.45 g/(L·h)。