DBT-ICT Centre for Energy Biosciences, Institute of Chemical Technology, Mumbai, Maharashtra, India.
Department of Chemical Engineering, Institute of Chemical Technology, Mumbai, Maharashtra, India.
Bioresour Technol. 2021 Apr;325:124636. doi: 10.1016/j.biortech.2020.124636. Epub 2020 Dec 30.
Docosahexaenoic acid (DHA) rich oil or biomass is currently being produced by fermentation of thraustochytrids by repeated fed-batch. Continuous cultivation has not been successful for DHA production because of excess carbon and limited nitrogen conditions requirement. The present study describes an alternative integrative fermentation strategy to simultaneously produce high cell density, lipids and DHA in continuous mode for Aurantiochytrium limacinum. The high cell density system (≥120 g/L DCW basis) on carbon feeding led to DHA productivity of 0.508 g/L.h on poultry waste based medium with a process time of 48-54 h. The strategy integrates the advantages of repeated fed-batch for high cell densities and DHA content in continuous cultivation.
二十二碳六烯酸(DHA)丰富的油或生物质目前通过重复分批发酵法由厚壁菌门发酵生产。由于过量的碳和有限的氮条件要求,连续培养法在 DHA 生产方面并不成功。本研究描述了一种替代的整合发酵策略,用于在连续模式下同时生产高脂肪密度、脂质和 DHA 的金黄游动放线菌。基于禽畜废物的培养基上,高细胞密度系统(基于 DCW 基础≥120g/L)可实现高达 0.508g/L.h 的 DHA 生产力,工艺时间为 48-54h。该策略整合了重复分批发酵法在连续培养法中用于生产高细胞密度和 DHA 含量的优势。