Luca Antonia Grebe, Christina Maria Krekel, Constantin Alexander Maaß, Mario Beckers, Martin Smotrycki, An N. T. Phan, Lars M. Blank, Katharina Saur, Marcel Mann, Jörn Viell, Andreas Jupke, Jørgen Barsett Magnus
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However, it faces challenges from high osmolality, growth inhibitors, and predetermined substrate composition during fermentation, as well as elevated pigmentation that complicates downstream processing. Moreover, the separation techniques typically used for highly polar carboxylic acids face considerable yield limitations due to the high solubility of malic acid and its salts.</p><h3>Results</h3><p>This study developed an all-encompassing production process for malic acid from untreated sugar beet molasses. Fermentative malic acid production with <i>Ustilago trichophora</i> was investigated in batch, fed-batch, and pulsed batch in shake flask scale, followed by a scale-up into 150 L pilot scale. A total of 15.7 kg malic acid was produced in a repeated pulsed batch with membrane-based cell retention with a titer of 108 g/L, a yield of 0.50 g/g, and a space–time yield of 0.66 g/L/h (max. 1.1 g/L/h). 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引用次数: 0
摘要
背景:对化石基化学品的可持续替代品的需求不断增长,增加了人们对来自可再生生物质来源的平台化学品的兴趣,如苹果酸。该C4二羧酸在食品、医药、生物塑料等领域具有广泛的应用潜力。可持续平台化学品在商业上仍然缺乏竞争力,主要是由于高基材成本驱动的高生产成本。微生物生产使用更具成本效益的原料,如甜菜糖蜜,显示出前景。然而,它面临着来自高渗透压、生长抑制剂和发酵过程中预先确定的底物组成的挑战,以及使下游加工复杂化的色素沉着升高。此外,由于苹果酸及其盐的高溶解度,通常用于高极性羧酸的分离技术面临相当大的收率限制。结果:本研究开发了以未经处理的甜菜糖蜜为原料生产苹果酸的全面工艺。在摇瓶规模下研究了毛霉发酵生产苹果酸的分批、补料分批和脉冲分批,然后扩大到150 L中试规模。重复脉冲批法制备苹果酸15.7 kg,膜基细胞保留,滴度为108 g/L,产率为0.50 g/g,空时产率为0.66 g/L/h。1.1 g / L / h)。此外,副产物琥珀酸的浓度高达22.9 g/L。在随后的下游工艺中,活性炭用于两阶段的产品捕获,溶剂变化和脱色,然后是产品苹果酸和琥珀酸的结晶。根据实验结果,建立了一个Aspen Plus模型,以估计每克蔗糖当量0.43 g苹果酸(纯度为98%)和0.10 g琥珀酸的总体工艺收率。技术经济分析表明,生产成本在当前市场价格的范围内。结论:农业残留物流通常被认为是发酵平台化学品生产的成本效益替代品,尽管所解决的挑战阻碍了从已建立的有机酸生产中直接转移工艺策略。通过提出一种明确针对从未经处理的糖蜜中生产苹果酸的整体方法,这项工作证明了该开发过程在有意义的规模上的技术经济可行性。
From beet molasses to malic acid: holistic development of fermentation and downstream process
Background
The growing demand for sustainable alternatives to fossil-based chemicals has increased interest in platform chemicals derived from renewable biomass sources, such as malic acid. This C4 dicarboxylic acid is valued for its diverse application potential in food, pharmaceuticals, and bioplastics. Sustainable platform chemicals remain commercially uncompetitive primarily due to high production costs driven by high substrate costs. Microbial production using more cost-effective feedstocks like sugar beet molasses shows promise. However, it faces challenges from high osmolality, growth inhibitors, and predetermined substrate composition during fermentation, as well as elevated pigmentation that complicates downstream processing. Moreover, the separation techniques typically used for highly polar carboxylic acids face considerable yield limitations due to the high solubility of malic acid and its salts.
Results
This study developed an all-encompassing production process for malic acid from untreated sugar beet molasses. Fermentative malic acid production with Ustilago trichophora was investigated in batch, fed-batch, and pulsed batch in shake flask scale, followed by a scale-up into 150 L pilot scale. A total of 15.7 kg malic acid was produced in a repeated pulsed batch with membrane-based cell retention with a titer of 108 g/L, a yield of 0.50 g/g, and a space–time yield of 0.66 g/L/h (max. 1.1 g/L/h). In addition, the byproduct succinic acid was detected in concentrations of up to 22.9 g/L. In the subsequent downstream processing, activated carbons were used for two-stage product capture, solvent change, and decolorization, followed by crystallization of the products malic acid and succinic acid. Based on experimental results, an Aspen Plus model was developed to estimate the overall process yields of 0.43 g malic acid (98% purity) and 0.10 g succinic acid per gram sucrose equivalent. A techno-economic analysis suggests production costs within the range of current market prices.
Conclusion
Agricultural residue streams are often proposed as cost-effective alternatives for fermentative platform chemical production, although the challenges addressed hamper the direct transfer of process strategies from established organic acid production. By presenting a holistic approach explicitly tailored to malic acid production from untreated molasses, this work demonstrates the techno-economic feasibility of the developed process at a meaningful scale.
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