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在新型生物反应器中生产高粘度多糖甲基聚糖。

Production of a high viscosity polysaccharide, methylan, in a novel bioreactor.

作者信息

Oh D K, Kim J H, Yoshida T

机构信息

Department of Food Science and Technology, Woosuk University, Cheonju 565-800, Korea.

出版信息

Biotechnol Bioeng. 1997 Apr 20;54(2):115-21. doi: 10.1002/(SICI)1097-0290(19970420)54:2<115::AID-BIT3>3.0.CO;2-O.

Abstract

The effect of shear stress on the production of a high viscosity polysaccharide, methylan, from methanol by Methylobacterium organophilum was investigated by using a multidisk mixer. It was observed in the multidisk mixer with defined shear stresses that the specific production rate of methylan increased gradually with increasing shear stress up to 30 Pa, and the production rate was constant beyond 30 Pa. This result suggested that the limited mass transfer from the medium into cells reduced methylan production. A novel bioreactor that provided the large volume of a high shear region was used to increase methylan production. Fed-batch cultures in the novel bioreactor were performed by the dissolved oxygen-stat method of methanol. When 1.13 g/L ammonium ion was added, the concentrations of cells of methylan were 31 and 20.6 g/L, respectively. The productions of cells and methylan in our designed bioreactor were 20 and 50% higher than those obtained in a conventional fermentor. The methylan content reached a maximum of 20.7 g/L in the bioreactor and the viscosity of the fermentation broth was 127 Pa . s, which corresponds to 68 g/L as a xanthan.

摘要

使用多盘混合器研究了剪切应力对嗜有机甲基杆菌从甲醇生产高粘度多糖甲基聚糖的影响。在具有确定剪切应力的多盘混合器中观察到,甲基聚糖的比生产速率随着剪切应力增加至30 Pa而逐渐增加,超过30 Pa后生产速率保持恒定。该结果表明,从培养基到细胞的有限传质降低了甲基聚糖的产量。使用一种能提供大量高剪切区域的新型生物反应器来提高甲基聚糖的产量。在新型生物反应器中通过甲醇的溶解氧恒态法进行分批补料培养。当添加1.13 g/L铵离子时,甲基聚糖的细胞浓度分别为31 g/L和20.6 g/L。在我们设计的生物反应器中细胞和甲基聚糖的产量比传统发酵罐中的产量分别高出20%和50%。生物反应器中甲基聚糖含量最高达到20.7 g/L,发酵液粘度为127 Pa·s,相当于68 g/L的黄原胶。

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