Liu Han, Tian Mengzhen, Dong Ping, Zhao Yunying, Deng Yu
School of Biotechnology and Key Laboratory of Industrial Biotechnology of Ministry of Education, Jiangnan University, 1800 Lihu Road, Wuxi, Jiangsu 214122, China.
National Engineering Research Center of Cereal Fermentation and Food Biomanufacturing, Jiangnan University, 1800 Lihu Road, Wuxi, Jiangsu 214122, China.
ACS Synth Biol. 2025 Apr 18;14(4):1277-1287. doi: 10.1021/acssynbio.5c00005. Epub 2025 Apr 7.
Malonic acid (MA) is a high-value chemical with diverse applications in the fields of food, agriculture, medicine, and chemical synthesis. Despite the successful biosynthesis of MA has been performed in , , and , the resulting MA titers remain insufficient for industrial-scale production. In this study, three distinct metabolic pathways were designed and constructed to increase MA production in . Among these, the fumaric acid pathway comprising four key enzymes including the aspartase (AspA), the decarboxylase (PanD), the β-alanine-pyruvate transaminase (Pa0132), and the succinic aldehyde dehydrogenase (YneI) was identified as the most effective for MA production. Additionally, the supplementation of fumaric acid was found to significantly improve MA production. To further enhance the MA production, metabolic engineering strategies were employed, including the deletion of the gene, responsible for encoding the malonic semialdehyde reductase, and the gene, which encodes a glucose transporter. Finally, through the optimization of fermentation conditions and feeding strategies, the engineered strain achieved an MA titer of 1.4 g/L in shake flask and 17.8 g/L in fed-batch fermentation. This study provides new insights into the industrial-scale production of MA utilizing the metabolically engineered cells.
丙二酸(MA)是一种高价值化学品,在食品、农业、医药和化学合成等领域有多种应用。尽管已在[具体生物]、[具体生物]和[具体生物]中成功进行了MA的生物合成,但所得的MA滴度仍不足以进行工业规模生产。在本研究中,设计并构建了三种不同的代谢途径以提高[具体生物]中MA的产量。其中,由四种关键酶组成的富马酸途径,包括天冬氨酸酶(AspA)、脱羧酶(PanD)、β-丙氨酸-丙酮酸转氨酶(Pa0132)和琥珀醛脱氢酶(YneI),被确定为对MA生产最有效的途径。此外,发现添加富马酸可显著提高MA产量。为进一步提高MA产量,采用了代谢工程策略,包括删除负责编码丙二酸半醛还原酶的[具体基因]和编码葡萄糖转运蛋白的[具体基因]。最后,通过优化发酵条件和补料策略,工程菌株在摇瓶中MA滴度达到1.4 g/L,在分批补料发酵中达到17.8 g/L。本研究为利用代谢工程改造的[具体生物]细胞进行MA的工业规模生产提供了新的见解。