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利用代谢工程化的氧化葡萄糖酸杆菌在低成本盐培养基中高效生产接近理论最大产率的光学纯 D-(-)-乳酸,对甘蔗渣进行技术经济评估。

Techno-economical valorization of sugarcane bagasse for efficiently producing optically pure D-(-)-lactate approaching the theoretical maximum yield in low-cost salt medium by metabolically engineered Klebsiella oxytoca.

机构信息

Metabolic Engineering Research Unit, School of Biotechnology, Institute of Agricultural Technology, Suranaree University of Technology, 111 University Avenue, Suranaree Sub-district, Muang District, Nakhon Ratchasima 30000, Thailand.

Metabolic Engineering Research Unit, School of Biotechnology, Institute of Agricultural Technology, Suranaree University of Technology, 111 University Avenue, Suranaree Sub-district, Muang District, Nakhon Ratchasima 30000, Thailand.

出版信息

Bioresour Technol. 2024 Sep;407:131145. doi: 10.1016/j.biortech.2024.131145. Epub 2024 Jul 21.

Abstract

Sugarcane bagasse (SCB) was utilized for efficiently producing optically pure D-(-)-lactate by Klebsiella oxytoca KIS004-91T strain. Cellulase (15 U/g NaOH-treated SCB) sufficiently liberated high sugars with saccharifications of 79.8 % cellulose and 52.5 % hemicellulose. For separated hydrolysis and fermentation, D-(-)-lactate was produced at 53.5 ± 2.1 g/L (0.98 ± 0.01 g/g sugar utilized or 0.71 ± 0.01 g/g total sugars) while D-(-)-lactate at 47.2 ± 1.8 g/L (0.78 ± 0.03 g/g sugar used or 0.69 ± 0.01 g/g total sugars) was obtained under simultaneous saccharification and fermentation (SSF). D-(-)-lactate at 99.9 ± 0.9 g/L (0.97 ± 0.01 g/g sugar utilized or 0.78 ± 0.01 g/g total sugars) was improved via fed-batch SSF. Based on mass balance, raw SCB of 7 kg is required to produce 1 kg D-(-)-lactate. Unlike others, D-(-)-lactate production was performed in low-cost salt medium without requirements of rich nutrients. Costs regarding medium, purification, and waste disposal may be reduced. This unlocks economic capability of SCB bioconversion or agricultural and agro-industrial wastes into high valuable D-(-)-lactate.

摘要

利用氧化葡萄糖酸杆菌 KIS004-91T 菌株从甘蔗渣中高效生产光学纯 D-(-)-乳酸。纤维素酶(NaOH 处理的甘蔗渣 15 U/g)充分释放了高糖,纤维素糖化率为 79.8%,半纤维素糖化率为 52.5%。为了进行分离水解和发酵,在分批水解和发酵(HSF)中生产了 53.5±2.1 g/L 的 D-(-)-乳酸(0.98±0.01 g/g 糖利用或 0.71±0.01 g/g 总糖),而在同步糖化和发酵(SSF)中生产了 47.2±1.8 g/L 的 D-(-)-乳酸(0.78±0.03 g/g 糖利用或 0.69±0.01 g/g 总糖)。通过分批补料 SSF 将 D-(-)-乳酸提高到 99.9±0.9 g/L(0.97±0.01 g/g 糖利用或 0.78±0.01 g/g 总糖)。基于质量平衡,生产 1 公斤 D-(-)-乳酸需要 7 公斤原始甘蔗渣。与其他方法不同,D-(-)-乳酸的生产是在低成本盐培养基中进行的,不需要丰富的营养物质。可能会降低培养基、纯化和废物处理的成本。这释放了将甘蔗渣生物转化或农业和农业工业废物转化为高价值 D-(-)-乳酸的经济能力。

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