Ortiz Tena Franziska, Ranglová Karolína, Kubač David, Steinweg Christian, Thomson Claudia, Masojidek Jiří, Posten Clemens
Institute of Process Engineering in Life Sciences Karlsruhe Institute of Technology (KIT) Karlsruhe Germany.
Laboratory of Algal Biotechnology Centre Algatech Czech Academy of Science Institute of Microbiology Třeboň Czech Republic.
Eng Life Sci. 2021 Sep 12;21(10):607-622. doi: 10.1002/elsc.202100052. eCollection 2021 Oct.
The present work characterizes a submerged aerated hollow fiber polyvinylidene fluorid (PVDF) membrane (0.03 μm) device () designed for the ultrafiltration (UF) of microalgae suspensions. Commercial baker's yeast served as model suspension to investigate the influence of the aeration rate of the hollow fibers on the critical flux (CF, ) for different cell concentrations. An optimal aeration rate of 1.25 vvm was determined. Moreover, the CF was evaluated using two different cultures (axenic and non-axenic) of various biomass densities (0.8-17.5 g DW/L). Comparably high CFs of 15.57 and 10.08 L/m//h were measured for microalgae concentrations of 4.8 and 10.0 g DW/L, respectively, applying very strict CF criteria. Furthermore, the -values correlated (negative) linearly with the biomass concentration (0.8-10.0 g DW/L). Concentration factors between 2.8 and 12.4 and volumetric reduction factors varying from 3.5 to 11.5 could be achieved in short-term filtration, whereat a stable filtration handling biomass concentrations up to 40.0 g DW/L was feasible. Measures for fouling control (aeration of membrane fibers, periodic backflushing) have thus been proven to be successful. Estimations on energy consumption revealed very low energy demand of 17.97 kJ/m treated microalgae feed suspension (4.99 × 10 kWh/m) and 37.83 kJ/kg treated biomass (1.05 × 10 kWh/kg), respectively, for an up-concentration from 2 to 40 g DW/L of a microalgae suspension.
本研究对一种用于微藻悬浮液超滤(UF)的浸没式曝气中空纤维聚偏氟乙烯(PVDF)膜(0.03μm)装置进行了表征。使用商业面包酵母作为模型悬浮液,研究中空纤维曝气速率对不同细胞浓度下临界通量(CF, )的影响。确定了1.25vvm的最佳曝气速率。此外,使用两种不同生物量密度(0.8 - 17.5g干重/L)的培养物(无菌和非无菌)评估了CF。在采用非常严格的CF标准时,分别测得微藻浓度为4.8和10.0g干重/L时的CF相当高,分别为15.57和10.08L/m²/h。此外, 值与生物量浓度(0.8 - 10.0g干重/L)呈线性(负)相关。在短期过滤中,可以实现2.8至12.4的浓缩因子和3.5至11.5的体积减少因子,在这种情况下,稳定过滤处理高达40.0g干重/L的生物量浓度是可行的。因此,已证明污垢控制措施(膜纤维曝气、定期反冲洗)是成功的。能耗估计表明,将微藻悬浮液从2g干重/L浓缩至40g干重/L时,处理微藻进料悬浮液的能耗非常低,分别为17.97kJ/m²(4.99×10⁻³kWh/m²)和处理生物量的能耗为37.83kJ/kg(1.05×10⁻²kWh/kg)。