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Dynamic and local gas holdup studies in external loop recirculating airlift reactor with two rolls of fiberglass packing using electrical resistance tomography

机译:使用电阻层析成像技术研究两卷玻璃纤维盘根外循环循环气举反应器中的动态和局部气体滞留率

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BACKGROUND: Airlift bioreactors have been used extensively in biotechnology industries in recent years in a variety of arrangements and applications. The insertion of packing inside the bioreactors has the potential to provide high productivity within a compact size through utilizing immobilized species. RESULTS: A novel recirculating external loop airlift bioreactor that has two rolls of fiberglass packing and a gas distributor in between was designed and built. Electrical resistance tomography (ERT) images showed that the gas holdup increased after installing the packing and the gas distributor. Gas holdup in the riser increased with decreasing static liquid height in the bioreactor. This decreased the liquid superficial velocity, which contributed to a higher gas holdup in the bioreactor. Results also showed that riser gas holdup varied slightly with different sparger configurations. Higher gas holdup increases the oxygen mass transfer rate by increasing the residence time and interfacial mass transfer area. CONCLUSION: ERT results showed that fiberglass packing with an installed gas distributor in bioreactors can achieve higher gas holdup at higher superficial gas velocity. This can contribute to improved conversion in bioreactors with packing through utilizing higher biomass concentrations and higher oxygen concentration.
机译:背景技术:近年来,气举生物反应器已在生物技术行业中以各种布置和应用广泛使用。在生物反应器内部插入填料具有通过利用固定化的物种在紧凑的尺寸内提供高生产率的潜力。结果:设计并制造了一种新颖的循环外循环气举生物反应器,该反应器具有两卷玻璃纤维填料和一个气体分配器。电阻层析成像(ERT)图像显示,在安装填料和气体分配器后,气体滞留量增加。提升管中的气体滞留量随生物反应器中静态液体高度的降低而增加。这降低了液体的表面速度,从而导致了生物反应器中更高的气体滞留率。结果还表明,在不同的喷射器配置下,立管气体滞留量略有不同。较高的气体滞留量通过增加停留时间和界面传质面积来提高氧气的传质速率。结论:ERT结果表明,在生物反应器中安装了气体分配器的玻璃纤维填料可以在较高的表观气体速度下实现较高的气体滞留率。通过利用较高的生物质浓度和较高的氧浓度,这可以有助于改进具有填料的生物反应器中的转化率。

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