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首页> 外文期刊>Journal of industrial microbiology & biotechnology >Hydrodynamic characteristics and mixing behaviour of Sclerotium glucanicumculture fluids in an airlift reactor with an internal loop used forscleroglucan production
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Hydrodynamic characteristics and mixing behaviour of Sclerotium glucanicumculture fluids in an airlift reactor with an internal loop used forscleroglucan production

机译:硬核葡聚糖培养液在带有内部回路用于硬葡聚糖生产的气举反应器中的流体动力学特性和混合行为

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摘要

The filamentous fungus, Sclerotium glucanicum NRRL 3006, was cultivated in a 0.008 m(3) airlift bioreactor with internal recirculation loop (ARL-IL) for production of the biopolymer, scleroglucan. The rheological behaviour of the culture fluid was characterised by measurement of the fluid consistency coefficient (K) and the flow behaviour index (n). Based on these measurements, the culture fluid changed from a low viscosity Newtonian system early in the process, to a viscous non-Newtonian (pseudoplastic) system. In addition, reactor hydrodynamics and mixing behaviour were characterised by measurement of whole mean gas hold-up (epsilon (g)), liquid re-circulation velocity (U-ld) and mixing time (t(m)). Under identical process conditions, the effects of the viscosity of the culture fluid and airflow rate on epsilon (g), U-ld and t(m) were examined and empirical correlations for epsilon (g), U-ld and t(m) with both superficial velocity U-g and consistency coefficient K were obtained and expressed separately. The correlations obtained are likely to describe the behaviour of real fungal culture fluids more accurately than previous correlations based on Newtonian or simulated non-Newtonian systems.
机译:丝状真菌菌核菌(Sclerotium glucanicum NRRL 3006)在具有内部再循环回路(ARL-IL)的0.008 m(3)气举生物反应器中培养,用于生产生物聚合物菌核葡聚糖。通过测量流体稠度系数(K)和流动行为指数(n)来表征培养液的流变行为。根据这些测量结果,培养液从过程早期的低粘度牛顿体系变为粘性的非牛顿(假塑性)体系。此外,通过测量整体平均气体滞留量(ε(g)),液体再循环速度(U-ld)和混合时间(t(m))来表征反应器的流体动力学和混合行为。在相同的工艺条件下,检查了培养液的粘度和气流速率对ε(g),U-ld和t(m)的影响,并确定了ε(g),U-ld和t(m)的经验相关性分别获得了表观速度Ug和稠度系数K分别表示。所获得的相关性可能比基于牛顿或模拟非牛顿系统的先前相关性更准确地描述实际真菌培养液的行为。

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