Two-stage conversion of syngas and pyrolysis aqueous condensate into L-malate

IF 6.1 1区 工程技术 Q1 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Alberto Robazza, Flávio C. F. Baleeiro, Sabine Kleinsteuber, Anke Neumann
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引用次数: 0

Abstract

Hybrid thermochemical–biological processes have the potential to enhance the carbon and energy recovery from organic waste. This work aimed to assess the carbon and energy recovery potential of multifunctional processes to simultaneously sequestrate syngas and detoxify pyrolysis aqueous condensate (PAC) for short-chain carboxylates production. To evaluate relevant process parameters for mixed culture co-fermentation of syngas and PAC, two identical reactors were run under mesophilic (37 °C) and thermophilic (55 °C) conditions at increasing PAC loading rates. Both the mesophilic and the thermophilic process recovered at least 50% of the energy in syngas and PAC into short-chain carboxylates. During the mesophilic syngas and PAC co-fermentation, methanogenesis was completely inhibited while acetate, ethanol and butyrate were the primary metabolites. Over 90% of the amplicon sequencing variants based on 16S rRNA were assigned to Clostridium sensu stricto 12. During the thermophilic process, on the other hand, Symbiobacteriales, Syntrophaceticus, Thermoanaerobacterium, Methanothermobacter and Methanosarcina likely played crucial roles in aromatics degradation and methanogenesis, respectively, while Moorella thermoacetica and Methanothermobacter marburgensis were the predominant carboxydotrophs in the thermophilic process. High biomass concentrations were necessary to maintain stable process operations at high PAC loads. In a second-stage reactor, Aspergillus oryzae converted acetate, propionate and butyrate from the first stage into L-malate, confirming the successful detoxification of PAC below inhibitory levels. The highest L-malate yield was 0.26 ± 2.2 molL-malate/molcarboxylates recorded for effluent from the mesophilic process at a PAC load of 4% v/v. The results highlight the potential of multifunctional reactors where anaerobic mixed cultures perform simultaneously diverse process roles, such as carbon fixation, wastewater detoxification and carboxylates intermediate production. The recovered energy in the form of intermediate carboxylates allows for their use as substrates in subsequent fermentative stages.

将合成气和热解水冷凝物分两步转化为 L-苹果酸盐
热化学-生物混合工艺具有从有机废物中提高碳和能源回收的潜力。这项工作旨在评估多功能工艺的碳和能量回收潜力,以同时封存合成气和解毒热解水冷凝物(PAC),生产短链羧酸盐。为了评估合成气和 PAC 混合培养共同发酵的相关工艺参数,两个相同的反应器分别在嗜中性(37 °C)和嗜热性(55 °C)条件下运行,PAC 加载率不断增加。嗜中和嗜热过程都能将合成气和 PAC 中至少 50% 的能量回收为短链羧酸盐。在中嗜热合成气和 PAC 共同发酵过程中,甲烷生成被完全抑制,而乙酸、乙醇和丁酸则成为主要的代谢产物。超过 90% 基于 16S rRNA 的扩增子测序变体被归入严格意义上的梭状芽孢杆菌 12。另一方面,在嗜热过程中,共生杆菌属、合成乙酸杆菌属、嗜热杆菌属、甲烷热杆菌属和甲烷arcina 可能分别在芳烃降解和甲烷生成过程中发挥了关键作用,而热乙酸莫雷拉菌和马尔堡甲烷热杆菌则是嗜热过程中最主要的羧营养体。要在高 PAC 负荷下保持稳定的工艺运行,就必须有高浓度的生物质。在第二阶段反应器中,黑曲霉(Aspergillus oryzae)将第一阶段的乙酸盐、丙酸盐和丁酸盐转化为左旋苹果酸盐,证实了 PAC 在抑制水平以下成功解毒。在 PAC 含量为 4% v/v 时,中温工艺产生的废水中 L-苹果酸产量最高,为 0.26 ± 2.2 molL-苹果酸/摩尔羧酸盐。这些结果凸显了多功能反应器的潜力,在这种反应器中,厌氧混合培养物可同时发挥碳固定、废水解毒和羧酸盐中间体生产等多种工艺作用。以羧酸盐中间体形式回收的能量可在后续发酵阶段用作底物。
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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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