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Analyzing redox balance in a synthetic yeast platform to improve utilization of brown macroalgae as feedstock

机译:在合成酵母平台中分析氧化还原平衡,以提高棕色大型藻类作为原料的利用率

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Macroalgae have high potential to be an efficient, and sustainable feedstock for the production of biofuels and other more valuable chemicals. Attempts have been made to enable the co-fermentation of alginate and mannitol by Saccharomyces cerevisiae to unlock the full potential of this marine biomass. However, the efficient use of the sugars derived from macroalgae depends on the equilibrium of cofactors derived from the alginate and mannitol catabolic pathways. There are a number of strong metabolic limitations that have to be tackled before this bioconversion can be carried out efficiently by engineered yeast cells. An analysis of the redox balance during ethanol fermentation from alginate and mannitol by Saccharomyces cerevisiae using metabolic engineering tools was carried out. To represent the strain designed for conversion of macroalgae carbohydrates to ethanol, a context-specific model was derived from the available yeast genome-scale metabolic reconstructions. Flux balance analysis and dynamic simulations were used to determine the flux distributions. The model indicates that ethanol production is determined by the activity of 4-deoxy-l-erythro-5-hexoseulose uronate (DEHU) reductase (DehR) and its preferences for NADH or NADPH which influences strongly the flow of cellular resources. Different scenarios were explored to determine the equilibrium between NAD(H) and NADP(H) that will lead to increased ethanol yields on mannitol and DEHU under anaerobic conditions. When rates of mannitol dehydrogenase and DehR"N"A"D"H tend to be close to a ratio in the range 1-1.6, high growth rates and ethanol yields were predicted. The analysis shows a number of metabolic limitations that are not easily identified through experimental procedures such as quantifying the impact of the cofactor preference by DEHU reductase in the system, the low flux into the alginate catabolic pathway, and a detailed analysis of the redox balance. These results show that production of ethanol and other chemicals can be optimized if a redox balance is achieved. A possible methodology to achieve this balance is presented. This paper shows how metabolic engineering tools are essential to comprehend and overcome this limitation.
机译:大型藻类有潜力成为生产生物燃料和其他更有价值的化学品的有效,可持续的原料。尝试通过酿酒酵母使海藻酸盐和甘露醇共同发酵,以释放这种海洋生物质的全部潜力。然而,衍生自大型藻类的糖的有效利用取决于衍生自藻酸盐和甘露醇分解代谢途径的辅因子的平衡。在工程改造的酵母细胞可以有效地进行生物转化之前,必须解决许多强烈的代谢限制。使用代谢工程工具对酿酒酵母通过乙醇发酵从藻酸盐和甘露醇中进行的氧化还原平衡进行了分析。为了代表为将大藻类碳水化合物转化为乙醇而设计的菌株,从可用的酵母基因组规模的代谢重建中获得了背景特定模型。磁通平衡分析和动态模拟用于确定磁通分布。该模型表明,乙醇的产生取决于4-脱氧-1-赤藓基5-己糖醛酸酯(DEHU)还原酶(DehR)的活性及其对NADH或NADPH的偏好,NADH或NADPH强烈影响细胞资源的流动。探索了不同的场景来确定NAD(H)和NADP(H)之间的平衡,这将导致在厌氧条件下甘露醇和DEHU上乙醇的产量增加。当甘露醇脱氢酶和DehR“ N” A“ D” H的比率趋于接近1-1.6的比率时,预测了高生长速度和乙醇产率。该分析显示了许多代谢限制,这些代谢限制无法通过实验程序轻松确定,例如,量化DEHU还原酶对辅因子偏爱在系统中的影响,进入藻酸盐分解代谢途径的通量低以及对氧化还原平衡的详细分析。这些结果表明,如果实现氧化还原平衡,则可以优化乙醇和其他化学品的生产。提出了实现这种平衡的可能方法。本文展示了代谢工程工具对于理解和克服这一局限性至关重要。

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