Baig Muhammad Irshad, Pejman Mehdi, Willott Joshua D, Tiraferri Alberto, de Vos Wiebe M
Faculty of Science and Technology, Membrane Science and Technology, MESA+ Institute for Nanotechnology, University of Twente, P.O. Box 217, Enschede 7500 AE, The Netherlands.
Department of Environment, Land and Infrastructure Engineering (DIATI), Politecnico di Torino, Corso Duca degli Abruzzi 24, Turin 10129, Italy.
ACS Appl Polym Mater. 2022 Feb 11;4(2):1010-1020. doi: 10.1021/acsapm.1c01464. Epub 2022 Jan 11.
Hollow fiber (HF) membrane geometry is the preferred choice for most commercial membrane operations. Such fibers are conventionally prepared via the non-solvent-induced phase separation technique, which heavily relies on hazardous and reprotoxic organic solvents such as -methyl pyrrolidone. A more sustainable alternative, i.e., aqueous phase separation (APS), was introduced recently that utilizes water as a solvent and non-solvent for the production of polymeric membranes. Herein, for the first time, we demonstrate the preparation of sustainable and functional HF membranes via the APS technique in a dry-jet wet spinning process. The dope solution comprising poly(sodium 4-styrenesulfonate) (PSS) and polyethyleneimine (PEI) at high pH along with an aqueous bore liquid is pushed through a single orifice spinneret into a low pH acetate buffer coagulation bath. Here, PEI becomes charged resulting in the formation of a polyelectrolyte complex with PSS. The compositions of the bore liquid and coagulation bath were systematically varied to study their effect on the structure and performance of the HF membranes. The microfiltration-type membranes (permeability ∼500 to 800 L·m·h·bar) with complete retention of emulsion droplets were obtained when the precipitation rate was slow. Increasing the concentration of the acetate buffer in the bath led to the increase in precipitation rate resulting in ultrafiltration-type membranes (permeability ∼12 to 15 L·m·h·bar) having molecular weight cut-offs in the range of ∼7.8-11.6 kDa. The research presented in this work confirms the versatility of APS and moves it another step closer to large-scale use.
中空纤维(HF)膜结构是大多数商业膜操作的首选。此类纤维传统上是通过非溶剂诱导相分离技术制备的,该技术严重依赖于危险且具有再毒性的有机溶剂,如N-甲基吡咯烷酮。最近引入了一种更具可持续性的替代方法,即水相分离(APS),它利用水作为溶剂和非溶剂来生产聚合物膜。在此,我们首次展示了通过APS技术在干喷湿纺过程中制备可持续且功能性的HF膜。将包含高pH值的聚(4-苯乙烯磺酸钠)(PSS)和聚乙烯亚胺(PEI)的纺丝溶液与水性内相液一起通过单孔喷丝头挤入低pH值的醋酸盐缓冲凝固浴中。在此,PEI带电,导致与PSS形成聚电解质复合物。系统地改变内相液和凝固浴的组成,以研究它们对HF膜结构和性能的影响。当沉淀速率较慢时,可获得完全保留乳液滴的微滤型膜(渗透率约为500至800 L·m⁻²·h⁻¹·bar⁻¹)。增加浴中醋酸盐缓冲液的浓度会导致沉淀速率增加,从而得到截留分子量在约7.8 - 11.6 kDa范围内的超滤型膜(渗透率约为12至15 L·m⁻²·h⁻¹·bar⁻¹)。这项工作中提出的研究证实了APS的多功能性,并使其更接近大规模应用。