Kunz Philipp, King Rudibert
Chair of Measurement and Control, Technische Universität Berlin, Berlin, Germany.
Front Microbiol. 2022 May 20;13:842249. doi: 10.3389/fmicb.2022.842249. eCollection 2022.
In technical fermentations, filamentous microorganisms are exposed to different forms of mechanical stress, among which shear stress is prevalent in turbulent broths. Whereas small-scale bioreactors allow for realistic turbulent flow field conditions, they are not well-suited to investigate the fungal response to shear stress in more detail, as they only reveal the integral effect of a highly dynamic stress stimulus. Therefore, the widely used model system for producing constant, but rather low shear forces, the parallel plate flow chamber, is extended in this work by adding a backward-facing step (BFS). The BFS induces vortex shedding in the wake of the step and brings out distinct areas of different shear stress levels at the bottom of the chamber where mycelia grow. This allows for a stress-dependent analysis of growing cells using a confocal laser-scanning microscope. As the real stress cannot be measured in the experiment, the wall shear stress is estimated numerically using computational fluid dynamics (CFD). As a first application of the experimental setup, the relative biomass concentration, the relative amount of secretory vesicles and the relative amount of the chosen product glucoamylase produced by the filamentous fungus were measured. The obtained area scans show homogeneous mycelia growth in areas of low stress and cloud-like patterns downstream of the predicted flow reattachment length where high shear stress dominates. Quantitative analysis of the time course suggests that the amount of available secretory vesicles inside of decreases when the shear stress is increased, despite that no significant differences in biomass production could be found. In contrast, the highest level of glucoamylase was reached for intermediate volumetric flow rates, i.e., levels of shear stress.
在工业发酵中,丝状微生物会受到不同形式的机械应力,其中剪切应力在湍流发酵液中普遍存在。虽然小型生物反应器能够实现逼真的湍流场条件,但它们并不适合更详细地研究真菌对剪切应力的响应,因为它们只能揭示高度动态应力刺激的整体效应。因此,在本研究中,通过添加一个后向台阶(BFS)对广泛用于产生恒定但较低剪切力的平行平板流动腔模型系统进行了扩展。BFS在台阶后方诱导涡旋脱落,并在菌丝体生长的腔室底部形成不同剪切应力水平的明显区域。这使得能够使用共聚焦激光扫描显微镜对生长中的细胞进行应力依赖性分析。由于实验中无法测量实际应力,因此使用计算流体动力学(CFD)对壁面剪切应力进行数值估计。作为实验装置的首次应用,测量了丝状真菌产生的相对生物量浓度、分泌囊泡的相对数量以及所选产物糖化酶的相对数量。获得的区域扫描显示,在低应力区域菌丝体生长均匀,而在预测的流动再附着长度下游的高剪切应力主导区域呈现云状图案。对时间进程的定量分析表明,尽管在生物量生产方面未发现显著差异,但当剪切应力增加时,细胞内可用分泌囊泡的数量会减少。相比之下,在中等体积流速即剪切应力水平下,糖化酶达到了最高水平。