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Harvesting of microalgae inoculum in culture medium by membrane ultrafiltration

机译:用膜超滤收割培养基中的微藻含量

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Harvesting is a crucial step as it can represent 20 to 30 % of the overall cost of the whole process of microalgae exploitation for various applications such as cosmetics, neutracetic, food or energy. Generally, microalgae components are recovered after biomass dewatering and drying. In order to minimize energy requirements recovery would have to be performed from wet biomass by low-cost and low energy requirements technologies. For membrane processes, where pumping is generally the main operating cost, the culture medium is eliminated by permeation through a semi-permeable membrane. In this study, the dynamic cross-flow filtrations were performed in terms of permeation flux and maximum cell concentration reachable. The use of dynamic filtration system where the shear rate was independent on the feed flow, allow to reach better flux. The extrapolation to zero flux showed that it would be theoretically possible to achieve up to a factor of concentration close to 1000 was 200 g DM. L−1 (gdry matter. L−1).
机译:收获是一个关键的一步,因为它可以代表微量血糖剥削整体成本的20%至30%,这些应用是化妆品,中性缩乳,食物或能量等各种应用。通常,在生物质脱水和干燥后回收微藻组分。为了最小化能量需求,必须通过低成本和低能量要求技术从湿生物质进行恢复。对于膜过程,其中泵送通常是主要操作成本,通过渗透通过半透膜来消除培养基。在该研究中,在渗透通量和最大细胞浓度可达的方面进行动态交叉流动过滤。使用动态过滤系统,其中剪切速率与进料流有独立,允许达到更好的助焊剂。外推到零通量表明,理论上可以实现高达1000的浓​​度率为200g DM。 L. -1 (Gdry ark。升 -1 )。

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