Separate hydrolysis and fermentation of softwood bark pretreated with 2-naphthol by steam explosion

IF 6.1 1区 工程技术 Q1 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Andreas Averheim, Stefan Stagge, Leif J. Jönsson, Sylvia H. Larsson, Mikael Thyrel
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引用次数: 0

Abstract

Background

2-Naphthol, a carbocation scavenger, is known to mitigate lignin condensation during the acidic processing of lignocellulosic biomass, which may benefit downstream processing of the resulting materials. Consequently, various raw materials have demonstrated improved enzymatic saccharification yields for substrates pretreated through autohydrolysis and dilute acid hydrolysis in the presence of 2-naphthol. However, 2-naphthol is toxic to ethanol-producing organisms, which may hinder its potential application. Little is known about the implications of 2-naphthol in combination with the pretreatment of softwood bark during continuous steam explosion in an industrially scalable system.

Results

The 2-naphthol-pretreated softwood bark was examined through spectroscopic techniques and subjected to separate hydrolysis and fermentation along with a reference excluding the scavenger and a detoxified sample washed with ethanol. The extractions of the pretreated materials with water resulted in a lower aromatic content in the extracts and stronger FTIR signals, possibly related to guaiacyl lignin, in the nonextractable residue when 2-naphthol was used during pretreatment. In addition, cyclohexane/acetone (9:1) extraction revealed the presence of pristine 2-naphthol in the extracts and increased aromatic content of the nonextractable residue detectable by NMR for the scavenger-pretreated materials. Whole-slurry enzymatic saccharification at 12% solids loading revealed that elevated saccharification recoveries after 48 h could not be achieved with the help of the scavenger. Glucose concentrations of 16.9 (reference) and 15.8 g/l (2-naphthol) could be obtained after 48 h of hydrolysis. However, increased inhibition during fermentation of the scavenger-pretreated hydrolysate, indicated by yeast cell growth, was slight and could be entirely overcome by the detoxification stage. The ethanol yields from fermentable sugars after 24 h were 0.45 (reference), 0.45 (2-naphthol), and 0.49 g/g (2-naphthol, detoxified).

Conclusion

The carbocation scavenger 2-naphthol did not increase the saccharification yield of softwood bark pretreated in an industrially scalable system for continuous steam explosion. On the other hand, it was shown that the scavenger's inhibitory effects on fermenting microorganisms can be overcome by controlling the pretreatment conditions to avoid cross-inhibition or detoxifying the substrates through ethanol washing. This study underlines the need to jointly optimize all the main processing steps.

通过蒸汽爆炸对用 2-萘酚预处理过的软木树皮进行单独水解和发酵。
背景:众所周知,2-萘酚是一种碳位清除剂,可在木质纤维素生物质的酸性加工过程中缓解木质素缩合,从而有利于所得材料的下游加工。因此,对于在 2-萘酚存在下通过自动水解和稀酸水解预处理的基质,各种原料的酶糖化产量都有所提高。然而,2-萘酚对乙醇生产生物有毒,这可能会阻碍其潜在应用。人们对 2-萘酚与软木树皮预处理相结合在可工业化扩展的连续蒸汽爆炸系统中的影响知之甚少:结果:通过光谱技术检测了经 2-萘酚预处理的软木树皮,并将其与不含清除剂的参照物和用乙醇洗涤的解毒样品一起分别进行水解和发酵。用水萃取预处理过的材料后,萃取物中的芳烃含量降低,而在预处理过程中使用 2-萘酚时,不可萃取残留物中的傅立叶变换红外光谱信号更强,这可能与愈创木脂有关。此外,环己烷/丙酮(9:1)萃取显示萃取物中存在原始的 2-萘酚,而对于清道夫预处理过的材料,核磁共振可检测到不可萃取残留物中的芳香族含量增加。在固体含量为 12% 的条件下进行全浆酶法糖化,结果表明,在清净剂的帮助下,48 小时后的糖化回收率无法提高。经过 48 小时的水解,可获得 16.9 克/升(参考)和 15.8 克/升(2-萘酚)的葡萄糖浓度。不过,酵母细胞的生长情况表明,经清除剂预处理的水解物在发酵过程中受到的抑制略有增加,解毒阶段可以完全克服这种抑制。24 小时后,可发酵糖的乙醇产量分别为 0.45 克/克(参照物)、0.45 克/克(2-萘酚)和 0.49 克/克(2-萘酚,解毒):结论:在可工业化扩展的连续汽爆系统中,碳化清除剂 2-萘酚并没有提高软木树皮预处理的糖化产率。另一方面,研究表明,通过控制预处理条件以避免交叉抑制或通过乙醇洗涤对底物进行解毒,可以克服清除剂对发酵微生物的抑制作用。这项研究强调了联合优化所有主要加工步骤的必要性。
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来源期刊
Biotechnology for Biofuels
Biotechnology for Biofuels 工程技术-生物工程与应用微生物
自引率
0.00%
发文量
0
审稿时长
2.7 months
期刊介绍: Biotechnology for Biofuels is an open access peer-reviewed journal featuring high-quality studies describing technological and operational advances in the production of biofuels, chemicals and other bioproducts. The journal emphasizes understanding and advancing the application of biotechnology and synergistic operations to improve plants and biological conversion systems for the biological production of these products from biomass, intermediates derived from biomass, or CO2, as well as upstream or downstream operations that are integral to biological conversion of biomass. Biotechnology for Biofuels focuses on the following areas: • Development of terrestrial plant feedstocks • Development of algal feedstocks • Biomass pretreatment, fractionation and extraction for biological conversion • Enzyme engineering, production and analysis • Bacterial genetics, physiology and metabolic engineering • Fungal/yeast genetics, physiology and metabolic engineering • Fermentation, biocatalytic conversion and reaction dynamics • Biological production of chemicals and bioproducts from biomass • Anaerobic digestion, biohydrogen and bioelectricity • Bioprocess integration, techno-economic analysis, modelling and policy • Life cycle assessment and environmental impact analysis
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