Center for Microalgal Biotechnology and Biofuels, Institute of Hydrobiology, Chinese Academy of Sciences, Wuhan 430072, China; Key Laboratory for Algal Biology, Institute of Hydrobiology, Chinese Academy of Sciences, Wuhan, Hubei 430072, China.
Center for Microalgal Biotechnology and Biofuels, Institute of Hydrobiology, Chinese Academy of Sciences, Wuhan 430072, China; Key Laboratory for Algal Biology, Institute of Hydrobiology, Chinese Academy of Sciences, Wuhan, Hubei 430072, China.
J Biosci Bioeng. 2019 Jul;128(1):103-109. doi: 10.1016/j.jbiosc.2019.01.007. Epub 2019 Feb 18.
Ultrafiltration membrane harvesting of Scenedesmus acuminatus was tested using alternative feed (AF) directions, i.e., bottom feed-top feed cycle and traditional bottom feed (BF). Both operations were investigated to compare the membrane performance and membrane fouling in microalgal harvesting process by scanning electron microscope (SEM), confocal laser scanning microscopy (CLSM) and Fourier transform infrared (FTIR). The results showed that when the AF was used with and without backwashing, average flux increased by 27.9% and 17.9%, respectively, comparing with BF (68 L m h) and the final dry weight reached 197 g L and 175.8 g L, respectively. Microalgal cell deposition on AF membrane was reduced from 1.44 × 10 cell cm on BF membrane to 7.12 × 10 cell cm on AF membrane, according to SEM observation. The protein and polysaccharides on the AF membrane surface were also reduced according to CLSM and FTIR analysis. Fouling analysis along the fiber length revealed that fouling was most severe at the top section for BF as a result of a lower shear rate at the outlet. AF operation generated dynamic filtration by frequently switching flow directions, increasing the shear rate at both the top and bottom of the fibers, and therefore filtration and clean process simultaneously provided good performance.
采用交替进料(AF)方向,即底部进料-顶部进料循环和传统的底部进料(BF),对集胞藻(Scenedesmus acuminatus)的超滤膜收获进行了测试。通过扫描电子显微镜(SEM)、共聚焦激光扫描显微镜(CLSM)和傅里叶变换红外(FTIR),对这两种操作进行了比较,以比较微藻收获过程中的膜性能和膜污染。结果表明,与 BF(68 L m h)相比,当使用和不使用反冲洗的 AF 时,平均通量分别增加了 27.9%和 17.9%,最终干重分别达到 197 g L 和 175.8 g L。根据 SEM 观察,AF 膜上的微藻细胞沉积从 BF 膜上的 1.44×10 个细胞 cm 减少到 AF 膜上的 7.12×10 个细胞 cm。根据 CLSM 和 FTIR 分析,AF 膜表面的蛋白质和多糖也减少了。沿纤维长度的污染分析表明,由于出口处的剪切速率较低,BF 处的顶部区域污染最严重。AF 操作通过频繁切换流方向产生动态过滤,增加了纤维顶部和底部的剪切速率,因此过滤和清洁过程同时提供了良好的性能。