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Improvement of mixing time, mass transfer, and power consumption in an external loop airlift photobioreactor for microalgae cultures

机译:改善微藻培养的外环气举光生物反应器中的混合时间,传质和功耗

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摘要

Longer mixing times and higher power consumption are common problems in the design of photobiore-actors. In this study, a vertical triangular external airlift loop photobioreactor was designed, constructed and operated for microalgae production studies. Gas feeding was performed by two spargers: one at the bottom of the hypotenuse (downcomer) and another at the bottom of the vertical side (riser). This configuration provided more effective countercurrent liquid-gas flow in the hypotenuse. The mass transfer coefficient, gas hold-up, mixing time, circulation time, dimensionless mixing time, bubble size, and volumetric power consumption were measured and optimized using response surface methodology. Investigations were carried out on the performance of the riser (the vertical side), downcomer (the hypotenuse), and separator. The countercurrent flow in the hypotenuse provided sufficient contact between gas and liquid phases, and increased mixing and mass transfer rates, in contrast to the results of previous studies. The promising results of this geometry were shorter mixing time and a significant decrease in volumetric power consumption in comparison with other configurations for photobioreac-tors.
机译:更长的混合时间和更高的功耗是光生物反应器设计中的常见问题。在这项研究中,设计,构建和运行了一个垂直的三角形外部气举环光生物反应器,用于微藻生产研究。气体进料由两个喷射器进行:一个在斜边的底部(下降管),另一个在垂直侧的底部(上升管)。这种配置在斜边提供了更有效的逆流液气流动。使用响应面方法对传质系数,气体滞留量,混合时间,循环时间,无因次混合时间,气泡大小和体积功耗进行了测量和优化。对立管(垂直侧),降液管(斜边)和分离器的性能进行了研究。与先前的研究结果相反,斜边中的逆流提供了气相和液相之间的充分接触,并增加了混合和传质速率。与其他类型的光生物反应器相比,这种几何形状的有希望的结果是混合时间更短,体积功耗显着降低。

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