内循环气升式生物反应器中两种固定化微生物的高含量低聚果糖生产

T.-J. Lin, Y.-C. Lee
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引用次数: 26

摘要

研究了海藻酸钙固定化日本曲霉和黑曲霉菌丝体在内循环气升式生物反应器中以蔗糖为原料生产高含量低聚果糖的工艺。褐藻酸钙对日本刺参和黑刺参菌丝的最佳吸附量分别为1%和7% (w/w)。将固定化黑霉菌丝体60 g加入3-L 300 g/L蔗糖溶液,气速为7.32 cm/s的反应器中,分批反应9 h,总FOS产量约为混合物总糖的55% (w/w)。为了去除生成的葡萄糖(β-d-果糖呋喃苷酶抑制剂),第二次固定化黑霉菌丝体颗粒的最佳投入量为315 g。加入葡萄糖氧化酶后,FOSs的总质量分数达到90% (w/w),转果糖基化的初始速率比不添加葡萄糖氧化酶时提高了近两倍。此外,考虑到葡萄糖氧化酶有足够的氧气供应,同时又不会产生过大的剪切应力而破坏固定化颗粒,建议将5.49 cm/s作为操作气速。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
High-content fructooligosaccharides production using two immobilized microorganisms in an internal-loop airlift bioreactor

Production of high-content fructooligosaccharides (FOSs) from sucrose using calcium alginate-immobilized mycelia of Aspergillus japonicus and Aspergillus niger in an internal-loop airlift bioreactor was investigated. The optimal entrapment of mycelia in A. japonicus and A. niger in calcium alginate were 1% and 7% (w/w), respectively. When 60 g of the immobilized mycelia of A. japonicus was supplied into the reactor filling with 3-L 300 g/L sucrose solution and gas velocity 7.32 cm/s, the total FOS production was about 55% (w/w) of total sugars in the mixture after a batch reaction for 9 h. To remove the generated glucose, an inhibitor of β-d-fructofuranosidase, the optimal input of the second immobilized A. niger mycelia particles was 315 g. With this input, the total FOSs mass fraction reached up to 90% (w/w) and the initial rate of transfructosylation was increased almost twice as without supplying glucose oxidase. In addition, 5.49 cm/s was suggested as the operating gas velocity for considering sufficient oxygen supply for glucose oxidase without generating excessive shear stress to damage the immobilized particles.

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