Harvesting of microalgae inoculum in culture medium by membrane ultrafiltration

T. Tran, Ha Thuong Dinh, T. Nguyen
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Abstract

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).
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膜超滤法收获培养基中微藻接种物
收获是至关重要的一步,因为它可以占微藻开发的各种应用,如化妆品,中性,食品或能源的整个过程的总成本的20%至30%。一般来说,微藻成分是在生物质脱水干燥后回收的。为了尽量减少能源需求,必须通过低成本和低能源需求的技术从湿生物质中进行回收。对于膜工艺来说,泵送通常是主要的操作成本,通过半透膜的渗透可以消除培养基。在本研究中,根据渗透通量和可达到的最大细胞浓度进行动态交叉流过滤。采用动态过滤系统,其中剪切速率独立于进料流量,允许达到更好的通量。对零通量的外推表明,理论上可以达到接近1000的浓度因子为200g DM. L−1(干物质)。L−1)。
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