Kashid Mohan, Ghosalkar Anand
a Department of Technology , Savitribai Phule Pune University , Pune , Maharashtra , India.
b Division of Praj Industries Ltd. , Praj Matrix R&D Center , Pune , India.
Prep Biochem Biotechnol. 2018 Mar 16;48(3):288-295. doi: 10.1080/10826068.2018.1425715. Epub 2018 Mar 1.
Fermentation of xylose from hydrolysate of acid-treated corn cob by Pichia stipitis is inhibited by acetic acid and lignin derivatives. In the present study, we have designed and implemented an immobilized cell culture for xylose to ethanol conversion from acid-treated corn cob hydrolysate without the removal of fermentation inhibitors. In this study, cultivations of suspended and immobilized Pichia were compared in terms of ethanol yield and productivity to investigate whether the cell immobilization could improve resistance to inhibitors. Cell immobilization clearly favored the fermentative metabolism in nondetoxified corn cob hydrolysate leading to an improvement of twofold ethanol productivity as compared to that achieved with suspension culture. Calcium alginate as an immobilization matrix was selected to immobilize Pichia cells. Concentrations of sodium alginate, calcium chloride, and fermentor agitation speed were optimized for ethanol production using statistical method. Statistical analysis showed that agitation speed had maximum influence on ethanol production by immobilized Pichia cells. In comparison to suspension culture, immobilization had a positive impact on the fermentative metabolism of Pichia, improving the ethanol yield from 0.40 to 0.43 g/g and productivity from 0.31 to 0.51 g/L/h for acid-treated corn cob hydrolysate.
树干毕赤酵母对酸处理玉米芯水解产物中木糖的发酵会受到乙酸和木质素衍生物的抑制。在本研究中,我们设计并实施了一种固定化细胞培养方法,用于在不去除发酵抑制剂的情况下将酸处理玉米芯水解产物中的木糖转化为乙醇。在本研究中,比较了悬浮态和固定化树干毕赤酵母培养物的乙醇产量和生产率,以研究细胞固定化是否能提高对抑制剂的耐受性。细胞固定化明显有利于未解毒玉米芯水解产物中的发酵代谢,与悬浮培养相比,乙醇生产率提高了两倍。选择海藻酸钙作为固定化基质来固定树干毕赤酵母细胞。使用统计方法对海藻酸钠、氯化钙浓度和发酵罐搅拌速度进行了乙醇生产优化。统计分析表明,搅拌速度对固定化树干毕赤酵母细胞的乙醇生产影响最大。与悬浮培养相比,固定化对树干毕赤酵母的发酵代谢有积极影响,酸处理玉米芯水解产物的乙醇产量从0.40 g/g提高到0.43 g/g,生产率从0.31 g/L/h提高到0.51 g/L/h。