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Modified alumina nanofiber membranes for protein separation

机译:用于蛋白质分离的改性氧化铝纳米纤维膜

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摘要

Large-scale purification/separation of bio-substances is a key technology required for rapid production of biological substances in bioengineering. Membrane filtration is a new separation process and has potential to be used for concentration (removal of solvent), desalting (removal of low molecular weight compounds), clarification (removal of particles), and fractionation (protein-protein separation). In this study, we developed an efficient membrane for protein separation based on ceramic nanofibers. Alumina nanofibers were prepared on a porous support and formed large flow passages. The radical changes in membrane structure provided new ceramic membranes with a large porosity (more than 70%) due to the replacement of bulk particles with fine fibers as building components. The pore size had an average of 11 nm and pure water flux was approximately 360 L•h-1•m-2•bar-1. Further surface modification with a self-assembled monolayer of (3-aminopropyl) triethoxysilane enhanced the membrane filtration properties. Characterization with SEM, FTIR, contact angle, and proteins separation tests indicated that the fibril layers uniformly spread on the surface of the porous support. Moreover, the membrane surface was changed from hydrophilic to hydrophobic after silane groups were grafted. It demonstrated that the silane-grafted alumina fiber membrane can reject 100% BSA protein and 92% cellulase protein. It was also able to retain 75% trypsin protein while maintaining a permeation flux of 48 L•h-1•m-2•bar-1.
机译:生物物质的大规模纯化/分离是生物工程中快速生产生物物质所需的关键技术。膜过滤是一种新的分离工艺,具有用于浓缩(去除溶剂),脱盐(去除低分子量化合物),澄清(去除颗粒)和分级分离(蛋白质-蛋白质分离)的潜力。在这项研究中,我们开发了一种基于陶瓷纳米纤维的高效蛋白质分离膜。在多孔载体上制备氧化铝纳米纤维,并形成大的流动通道。膜结构的根本变化为新型陶瓷膜提供了较大的孔隙率(超过70%),这是因为用细纤维代替了建筑材料中的散装颗粒。孔径平均为11 nm,纯水通量约为360 L•h-1•m-2•bar-1。用(3-氨基丙基)三乙氧基硅烷的自组装单层进行进一步的表面改性可增强膜过滤性能。用SEM,FTIR,接触角和蛋白质分离测试的表征表明,原纤维层均匀地铺展在多孔载体的表面上。此外,在接枝硅烷基团后,膜表面从亲水性变为疏水性。结果表明,硅烷接枝的氧化铝纤维膜可以排斥100%的BSA蛋白和92%的纤维素酶蛋白。它还能够保留75%的胰蛋白酶蛋白,同时保持48 L•h-1•m-2•bar-1的渗透通量。

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