Centre Energétique et Procédés (CEP), MINES ParisTech, Palaiseau, France.
Appl Microbiol Biotechnol. 2012 Jan;93(1):117-29. doi: 10.1007/s00253-011-3398-9. Epub 2011 Jun 28.
Internal airlift reactors are closed systems considered today for microalgae cultivation. Several works have studied their hydrodynamics but based on important solid concentrations, not with biomass concentrations usually found in microalgae cultures. In this study, an internal airlift reactor has been built and tested in order to clarify the hydrodynamics of this system, based on microalgae typical concentrations. A model is proposed taking into account the variation of air bubble velocity according to volumetric air flow rate injected into the system. A relationship between riser and downcomer gas holdups is established, which varied slightly with solids concentrations. The repartition of solids along the reactor resulted to be homogenous for the range of concentrations and volumetric air flow rate studied here. Liquid velocities increase with volumetric air flow rate, and they vary slightly when solids are added to the system. Finally, liquid circulation time found in each section of the reactor is in concordance with those employed in microalgae culture.
内部气升式反应器是目前被认为用于微藻培养的封闭系统。已有多项工作研究了其流体动力学,但这些研究都是基于较高的固体浓度,而不是微藻培养中常见的生物量浓度。在本研究中,为了阐明基于微藻典型浓度的该系统的流体动力学,构建并测试了一个内部气升式反应器。提出了一个模型,该模型考虑了根据注入系统的体积空气流量变化的气泡速度。建立了上升管和下降管的气体含率之间的关系,该关系随固体浓度的变化而略有变化。在所研究的浓度和体积空气流量范围内,固体在反应器中的分布是均匀的。液体速度随体积空气流量的增加而增加,当向系统中添加固体时,液体速度略有变化。最后,在反应器的每个部分中发现的液体循环时间与在微藻培养中使用的时间一致。