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Production of beta-glucan and related glucan-hydrolases by Botryosphaeria rhodina

机译:Rhodina Botryosphaeria rhodina生产β-葡聚糖和相关葡聚糖水解酶

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Aims: Characterization of beta-glucan production from Botryosphaeria rhodina DABAC-P82 by detecting simultaneously glucan-hydrolytic enzymes and their localization, culture medium rheology and oxygen transfer. Methods and Results: Mycelium growth, beta-glucan production, substrate consumption and glucan-hydrolytic enzymes were monitored both in shaken flasks and in a 3-l stirred-tank bioreactor. Glucan production (19.7 and 15.2 g l(-1), in flask and bioreactor, respectively) was accompanied by extra-cellular and cell-bound beta-glucanase and beta-glucosidase activities. In the bioreactor scale, in the time interval of 0-78 h the apparent viscosity of the culture broth exhibited a general increase; thereafter, it began to reduce, probably because of the above glucan-hydrolytic activities. Moreover, the culture media collected after 45 h behaved as solid-like materials at shear rates smaller than 0.001 s(-1), as pseudo-plastic liquids in the middle shear rate range and as Newtonian ones at shear rates greater than 1000 s(-1). Conclusion: The greatest beta-glucan accumulation in the bioreactor was found to be associated with nitrogen and dissolved oxygen concentrations smaller than 0.15 g l(-1) and 25%, respectively, and with the peak points of the glucan-degrading enzymes. Significance and Impact of the Study: A careful analysis of the critical factors (such as, culture broth rheology, oxygen mass transfer and glucan-hydrolytic enzymes) limiting the beta-glucan production by B. rhodina is a prerequisite to maximize beta-glucan yield and production, as well as to define the process flow sheet capable of maximizing biopolymer recovery, solvent re-utilization and glucose consumption.
机译:目的:通过同时检测葡聚糖水解酶及其定位,培养基的流变学和氧转移,来表征来自球形葡萄球菌DABAC-P82的β-葡聚糖生产。方法和结果:在摇瓶和3-l搅拌罐式生物反应器中监测菌丝体生长,β-葡聚糖产量,底物消耗和葡聚糖水解酶。葡聚糖的产生(分别在烧瓶和生物反应器中分别为19.7和15.2 g l(-1))伴随着细胞外和细胞结合的β-葡聚糖酶和β-葡糖苷酶的活性。在生物反应器规模上,在0-78 h的时间间隔内,培养液的表观粘度普遍增加;此后,它开始减少,可能是由于上述葡聚糖水解活性。此外,在45 h后收集的培养基在剪切速率小于0.001 s(-1)时表现为固体状,在中等剪切速率范围内表现为假塑性液体,在剪切速率大于1000 s(牛顿时)表现为牛顿液体。 -1)。结论:发现生物反应器中最大的β-葡聚糖积累与氮和溶解氧浓度分别小于0.15 g l(-1)和25%以及葡聚糖降解酶的峰值有关。研究的意义和影响:仔细分析限制红景天芽孢杆菌产生β-葡聚糖的关键因素(如培养液流变学,氧气传质和葡聚糖水解酶),这是最大化β-葡聚糖产量的前提条件和生产,以及定义能够最大化生物聚合物回收,溶剂再利用和葡萄糖消耗的工艺流程图。

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