Department of Civil and Environmental Engineering and Earth Sciences, University of Notre Dame, Notre Dame, Indiana, United States of America.
Department of Civil and Environmental Engineering, University of Pittsburgh, Pittsburgh, Pennsylvania, United States of America.
PLoS One. 2018 Jun 25;13(6):e0199104. doi: 10.1371/journal.pone.0199104. eCollection 2018.
Efficient conversion of cellulosic sugars in cellulosic hydrolysates is important for economically viable production of biofuels from lignocellulosic biomass, but the goal remains a critical challenge. The present study reports a new approach for simultaneous fermentation of cellobiose and xylose by using the co-culture consisting of recombinant Saccharomyces cerevisiae specialist strains. The co-culture system can provide competitive advantage of modularity compared to the single culture system and can be tuned to deal with fluctuations in feedstock composition to achieve robust and cost-effective biofuel production. This study characterized fermentation kinetics of the recombinant cellobiose-consuming S. cerevisiae strain EJ2, xylose-consuming S. cerevisiae strain SR8, and their co-culture. The motivation for kinetic modeling was to provide guidance and prediction of using the co-culture system for simultaneous fermentation of mixed sugars with adjustable biomass of each specialist strain under different substrate concentrations. The kinetic model for the co-culture system was developed based on the pure culture models and incorporated the effects of product inhibition, initial substrate concentration and inoculum size. The model simulations were validated by results from independent fermentation experiments under different substrate conditions, and good agreement was found between model predictions and experimental data from batch fermentation of cellobiose, xylose and their mixtures. Additionally, with the guidance of model prediction, simultaneous co-fermentation of 60 g/L cellobiose and 20 g/L xylose was achieved with the initial cell densities of 0.45 g dry cell weight /L for EJ2 and 0.9 g dry cell weight /L SR8. The results demonstrated that the kinetic modeling could be used to guide the design and optimization of yeast co-culture conditions for achieving simultaneous fermentation of cellobiose and xylose with improved ethanol productivity, which is critically important for robust and efficient renewable biofuel production from lignocellulosic biomass.
高效转化纤维素水解物中的纤维素糖对于从木质纤维素生物质经济地生产生物燃料非常重要,但这一目标仍然是一个关键挑战。本研究报告了一种使用由重组酿酒酵母专业菌株组成的共培养物同时发酵纤维二糖和木糖的新方法。与单一培养系统相比,共培养系统具有模块化的竞争优势,并且可以根据原料组成的波动进行调整,以实现稳健且具有成本效益的生物燃料生产。本研究对重组消耗纤维二糖的酿酒酵母菌株 EJ2、消耗木糖的酿酒酵母菌株 SR8 及其共培养物的发酵动力学进行了表征。进行动力学建模的动机是为使用共培养系统在不同底物浓度下,根据每个专业菌株的生物量可调,同时发酵混合糖提供指导和预测。共培养系统的动力学模型是基于纯培养模型开发的,并纳入了产物抑制、初始底物浓度和接种物大小的影响。通过在不同底物条件下进行独立发酵实验,对模型模拟进行了验证,在分批发酵纤维二糖、木糖及其混合物的实验数据与模型预测之间发现了很好的一致性。此外,在模型预测的指导下,以 0.45 g 干细胞重量/L 的初始 EJ2 细胞密度和 0.9 g 干细胞重量/L 的 SR8 初始细胞密度,实现了 60 g/L 纤维二糖和 20 g/L 木糖的同时共发酵。结果表明,动力学建模可用于指导酵母共培养条件的设计和优化,以实现纤维二糖和木糖的同时发酵,提高乙醇产率,这对于从木质纤维素生物质稳健且高效地生产可再生生物燃料至关重要。