用P-SSF工艺从碱处理的麦秆中生产纤维素乙醇及半纤维素馏分生物转化为高价值产品

Amisha Patel, Harshvadan Patel, Amita Shah
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引用次数: 1

摘要

木质纤维素生物质因其丰富且成本较低而成为生产乙醇的有吸引力的资源。通过提高乙醇滴度以及利用生物转化过程中产生的废物,可以提高木质纤维素乙醇生产的经济性。本研究旨在开发碱处理富纤维素麦秸(WS)生产高浓度乙醇的生物转化工艺,并将未利用的半纤维素部分转化为高附加值产品。采用微波辅助碱(MAA)对WS进行处理。扫描电镜和傅里叶变换红外光谱分析了未经处理和预处理的WS的结构变化。利用新分离的酿酒酵母(Saccharomyces cerevisisae) SM1,通过预水解和同步糖化发酵(P-SSF)工艺对预处理后的WS进行生物乙醇生产。预处理过程中产生的液体馏分利用本地生产的内生木聚糖酶生产低聚木糖(XOS)。MAA处理能通过增溶半纤维素和木质素来提高WS的纤维素含量。P-SSF法发酵48 h可获得高浓度乙醇(42.10±1.15 g/L),乙醇产率和产率分别为0.88 g/L/h和69.14%。可以预测,生产1吨乙醇可能需要7.143吨原料WS,同时还可以生产191.93千克木糖醇和263.58千克XOS (DP2 - DP5)。该研究表明,除了高乙醇产量外,生物精炼工艺还可以生产增值化合物。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Production of cellulosic ethanol from alkali treated wheat straw using P-SSF process and bioconversion of hemicellulosic fraction into high value products
Lignocellulosic biomass is an attractive resource for production of ethanol because of its abundance and lower cost. The economics of lignocellulosic ethanol production can be improved by enhancing the ethanol titres along with utilisation of waste generated during bioconversion process. The present study was aimed at development of a bioconversion process for production high concentration of ethanol from alkali treated cellulose rich wheat straw (WS) and utilization of unused hemicellulosic fraction into value added products. WS was subjected to microwave assisted alkali (MAA) treatment. Scanning electron microscopy and Fourier transform infrared spectroscopy were used to analyse structural changes in untreated and pretreated WS. Bioethanol production from pretreated WS was carried out by pre hydrolysis and simultaneous saccharification and fermentation (P-SSF) process using newly isolated Saccharomyces cerevisisae SM1. Liquid fraction generated during pretreatment was utilised for xylooligosaccharides (XOS) production using indigenously produced endoxylanase. MAA treatment of WS was successful in enriching cellulose content of WS by solubilizing hemicellulose and lignin. Ethanol fermentation by P-SSF method lead to high concentration of ethanol (42.10±1.15 g/L) in 48 h. Ethanol productivity and yield were, 0.88 g/L/h and 69.14%, respectively. It can be predicted that 7.143 tons of raw WS may be required to produce 1 ton of ethanol and for additional revenue 191.93 kg xylitol and 263.58 kg XOS (DP2 - DP5) can also be produced simultaneously. The study has demonstrated the feasibility of a bio-refinery process for production of value added compounds in addition to high ethanol yields.
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