首页> 美国卫生研究院文献>BioMed Research International >Optimization of Hydrothermal and Diluted Acid Pretreatments of Tunisian Luffa cylindrica (L.) Fibers for 2G Bioethanol Production through the Cubic Central Composite Experimental Design CCD: Response Surface Methodology
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Optimization of Hydrothermal and Diluted Acid Pretreatments of Tunisian Luffa cylindrica (L.) Fibers for 2G Bioethanol Production through the Cubic Central Composite Experimental Design CCD: Response Surface Methodology

机译:通过立方中心复合材料实验设计CCD优化突尼斯Luffa cylindrica(L.)纤维用于2G生物乙醇生产的水热和稀酸预处理的优化:响应面方法

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摘要

This paper opens up a new issue dealing with Luffa cylindrica (LC) lignocellulosic biomass recovery in order to produce 2G bioethanol. LC fibers are composed of three principal fractions, namely, α-cellulose (45.80%  ± 1.3), hemicelluloses (20.76%  ± 0.3), and lignins (13.15%  ± 0.6). The optimization of LC fibers hydrothermal and diluted acid pretreatments duration and temperature were achieved through the cubic central composite experimental design CCD. The pretreatments optimization was monitored via the determination of reducing sugars. Then, the 2G bioethanol process feasibility was tested by means of three successive steps, namely, LC fibers hydrothermal pretreatment performed at 96°C during 54 minutes, enzymatic saccharification carried out by means of a commercial enzyme AP2, and the alcoholic fermentation fulfilled with Saccharomyces cerevisiae. LC fibers hydrothermal pretreatment liberated 33.55 g/kg of reducing sugars. Enzymatic hydrolysis allowed achieving 59.4 g/kg of reducing sugars. The conversion yield of reducing sugar to ethanol was 88.66%. After the distillation step, concentration of ethanol was 1.58% with a volumetric yield about 70%.
机译:本文开辟了一个新的课题,涉及Luffa cylindrica(LC)木质纤维素生物质的回收,以生产2G生物乙醇。 LC纤维由三个主要部分组成,即α-纤维素(45.80%±1.3),半纤维素(20.76%±0.3)和木质素(13.15%±0.6)。通过立方中心复合实验设计CCD,实现了LC纤维水热和稀酸预处理的持续时间和温度的优化。通过确定还原糖来监测预处理的最优化。然后,通过三个连续步骤测试了2G生物乙醇工艺的可行性,即在96°C下进行54分钟的LC纤维水热预处理,通过商业化酶AP2进行酶促糖化以及通过酿酒酵母完成酒精发酵啤酒酵母。 LC纤维的水热预处理可释放33.55μg/ kg的还原糖。酶促水解可使还原糖达到59.4μg/ kg。还原糖向乙醇的转化率为88.66%。在蒸馏步骤之后,乙醇的浓度为1.58%,体积产率为约70%。

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