Valorization of milling byproducts and ergot-sclerotia-contaminated rye via clostridial ABE fermentation

IF 6.1 1区 工程技术 Q1 BIOTECHNOLOGY & APPLIED MICROBIOLOGY Biotechnology for Biofuels Pub Date : 2024-11-30 DOI:10.1186/s13068-024-02590-6
Holger Edelmann, Nils Thieme, Armin Ehrenreich, Vladimir Zverlov, Wolfgang Liebl
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Abstract

Background

Acetone–butanol–ethanol (ABE) fermentation by solventogenic clostridia can be harnessed to produce CO2 emission neutral bio-based 1-butanol, a valuable compound with a broad range of applications, e.g., in industrial production, as a solvent and as a fuel additive or replacement. However, the relatively low butanol titers and high feedstock costs prevent bio-butanol production on an industrial scale. Agricultural side-stream materials, like milling byproducts, are starch-rich, low-cost and produced all year round. They could be suitable substrates for bio-butanol production by ABE fermentation.

Results

The milling byproducts wheat red dog (WRD), rye second flour (RSF), wheat bran (WB), rye bran (RB) and ergot sclerotia-containing rye waste stream (ER) were found to contain between ~ 30 and ~ 85% glucan, most of which was starch based. WRD, RSF and ER had the highest glucan content, while the brans contained significant xylan concentrations. Four strains selected from the collection of solventogenic clostridia available in our group produced > 6 g/L butanol on the majority of these substrates, with Clostridium beijerinckii NCIMB 8052 showing the best ABE production performance when regarding all tested substrates. Toxic ergot sclerotia-containing waste material was found to be a suited substrate for ABE fermentation. Strain NCIMB 8052 exhibited butanol titers of up to 9 g/L on substrate mixtures of WRD plus ER and the highest butanol yield per used sugars. Finally, a semi-continuous ABE fermentation of C. beijerinckii NCIMB 8052 on WRD plus ER could be maintained for 96 h. The volumetric ABE productivity during the continuous phase of fermentation was ~ 0.41 g L−1 h−1 and a total of 37.7 g ABE was produced out of 168.2 g substrate.

Conclusions

Based on their carbohydrate composition, WRD, RSF and ER were the milling byproducts best suited as substrates for bio-butanol production by clostridial ABE fermentation. Importantly, also ergot sclerotia-containing waste materials can be used as substrates, which can help to reduce process costs. The semi-continuous fermentation showed that clostridial ABE fermentation on milling byproducts may represent a suitable avenue for commercial butanol production after further process and/or strain optimization.

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酵母ABE发酵制粉副产物及麦角菌污染黑麦的发酵研究
丙酮-丁醇-乙醇(ABE)通过溶剂性梭菌发酵可以生产二氧化碳排放中性生物基1-丁醇,这是一种有价值的化合物,具有广泛的应用,例如在工业生产中,作为溶剂和燃料添加剂或替代品。然而,相对较低的丁醇滴度和较高的原料成本阻碍了工业规模的生物丁醇生产。农业侧流材料,如碾磨副产品,富含淀粉,成本低,全年生产。它们可以作为ABE发酵生产生物丁醇的合适底物。结果制粉副产物小麦红狗(WRD)、黑麦二粉(RSF)、麦麸(WB)、黑麦麸皮(RB)和含麦角菌核的黑麦废液(ER)的葡聚糖含量在~ 30% ~ ~ 85%之间,其中葡聚糖以淀粉为主。WRD、RSF和ER的葡聚糖含量最高,而麸皮的木聚糖含量显著。从本小组收集的溶剂型梭菌中选择的4株菌株在大多数底物上产生6 g/L丁醇,其中北京氏梭菌NCIMB 8052在所有测试底物上表现出最好的ABE生产性能。发现含有毒麦角菌核的废料是ABE发酵的合适底物。菌株NCIMB 8052在WRD + ER的底物混合物上的丁醇滴度高达9 g/L,每使用糖的丁醇产量最高。结果表明,在WRD + ER条件下,贝氏弧菌NCIMB 8052半连续ABE发酵可维持96 h,连续发酵过程中ABE的体积产率为~ 0.41 g L−1 h−1,每168.2 g底物可产生37.7 g ABE。结论从其碳水化合物组成来看,WRD、RSF和ER是最适合作为ABE发酵生产生物丁醇底物的发酵副产物。重要的是,含有麦角菌核的废料也可以用作底物,这有助于降低工艺成本。半连续发酵表明,在进一步的工艺和/或菌株优化后,对铣削副产物进行ABE发酵可能是一种合适的商业丁醇生产途径。
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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
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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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