Ilyas Shazia, de Grooth Joris, Nijmeijer Kitty, de Vos Wiebe M
Membrane Science and Technology, MESA+ Institute for Nanotechnology, University of Twente, Faculty of Science and Technology, P.O. Box 217, 500 AE Enschede, The Netherlands.
Membrane Science and Technology, MESA+ Institute for Nanotechnology, University of Twente, Faculty of Science and Technology, P.O. Box 217, 500 AE Enschede, The Netherlands.
J Colloid Interface Sci. 2015 May 15;446:386-93. doi: 10.1016/j.jcis.2014.12.019. Epub 2014 Dec 16.
This manuscript investigates the modification of an ultra-filtration (UF) membrane support with polyelectrolyte multilayers (PEMs) consisting of the weak polyelectrolytes poly(allyl amine) hydrochloride (PAH) and poly(acrylic acid) (PAA). These prepared polyelectrolyte multilayer membranes have a dual function: They act as nanofiltration (NF) membranes and as sacrificial layers to allow easy cleaning of the membranes. In order to optimize the conditions for PEM coating and removal, adsorption and desorption of these layers on a model surface (silica) was first studied via optical reflectometry. Subsequently, a charged UF membrane support was coated with a PEM and after each deposited layer, a clear increase in membrane resistance against pure water permeation and a switch of the zeta potential were observed. Moreover these polyelectrolyte multilayer membranes, exhibited rejection of solutes in a range typical for NF membranes. Monovalent ions (NaCl) were hardly rejected (<24%), while rejections of >60% were observed for a neutral organic molecule sulfamethoxazole (SMX) and for the divalent ion SO3(2-). The rejection mechanism of these membranes seems to be dominated by size-exclusion. To investigate the role of these PEMs as sacrificial layers for the cleaning of fouled membranes, the prepared polyelectrolyte multilayers were fouled with silica nano particles. Subsequent removal of the coating using a rinse and a low pressure backwash with pH 3, 3M NaNO3 allowed for a drop in membrane resistance from 1.7⋅10(14)m(-1) (fouled membrane) to 9.9⋅10(12)m(-1) (clean membrane), which is nearly equal to that of the pristine membrane (9.7⋅10(12)m(-1)). Recoating of the support membrane with the same PEMs resulted in a resistance equal to the resistance of the original polyelectrolyte multilayer membrane. Interestingly, less layers were needed to obtain complete foulant removal from the membrane surface, than was the case for the model surface. The possibility for backwashing allows for an even more successful use of the sacrificial layer approach in membrane technology than on model surfaces. Moreover, these PEMs can be used to provide a dual function, as NF membranes and as a Sacrificial coating to allow easy membrane cleaning.
本手稿研究了用由弱聚电解质聚(烯丙胺)盐酸盐(PAH)和聚(丙烯酸)(PAA)组成的聚电解质多层膜(PEMs)对超滤(UF)膜载体进行改性。这些制备的聚电解质多层膜具有双重功能:它们既作为纳滤(NF)膜,又作为牺牲层,以便于膜的清洗。为了优化PEM涂层和去除的条件,首先通过光学反射法研究了这些层在模型表面(二氧化硅)上的吸附和解吸。随后,用PEM涂覆带电的UF膜载体,在每沉积一层后,观察到膜对纯水渗透的阻力明显增加以及zeta电位的转变。此外,这些聚电解质多层膜对溶质的截留率在NF膜典型的范围内。单价离子(NaCl)几乎不被截留(<24%),而对于中性有机分子磺胺甲恶唑(SMX)和二价离子SO3(2-),截留率观察到>60%。这些膜的截留机制似乎主要由尺寸排阻主导。为了研究这些PEMs作为牺牲层对污染膜进行清洗的作用,用二氧化硅纳米颗粒污染制备的聚电解质多层膜。随后使用pH为3的冲洗液和3M NaNO3进行低压反冲洗来去除涂层,使膜阻力从1.7⋅10(14)m(-1)(污染膜)降至9.9⋅10(12)m(-1)(清洁膜),这几乎与原始膜的阻力(9.7⋅10(12)m(-1))相等。用相同的PEMs对支撑膜进行重新涂覆,得到的阻力与原始聚电解质多层膜的阻力相等。有趣的是,与模型表面相比,从膜表面完全去除污垢所需的层数更少。反冲洗的可能性使得牺牲层方法在膜技术中的应用比在模型表面上更成功。此外,这些PEMs可用于提供双重功能,既作为NF膜,又作为牺牲涂层以便于膜的清洗。