Superhydrophobic composite graphene oxide membrane coated with fluorinated silica nanoparticles for hydrogen isotopic water separation in membrane distillation

膜蒸馏 石墨烯 渗透 氧化物 化学工程 材料科学 纳米颗粒 化学 纳米技术 海水淡化 生物化学 工程类 冶金
作者
Ming Wen,Min Chen,Kelin Chen,Pei-Long Li,Chao Lv,Xin Zhang,Yong Yao,Wan Yang,Guoqiang Huang,Guang-Kun Ren,Shunjie Deng,Yinke Liu,Zhe Zheng,Cigang Xu,Deli Luo
出处
期刊:Journal of Membrane Science [Elsevier BV]
卷期号:626: 119136-119136 被引量:30
标识
DOI:10.1016/j.memsci.2021.119136
摘要

Due to the laminar structure constructed by two-dimensional nanosheets, nanochannels are formed in the graphene oxide membrane (GOM), including capillaries formed by two closely spaced graphene sheets and nanopores in the nanosheets. These nanochannels have strong molecular sieving properties that can be tuned by various methods and applied in molecules separation. Such membranes are often used for the separation of different molecules or ions, but are rarely used for the isotope separation. In this work, superhydrophobic modification of the GOM was achieved by introducing layers of fluorinated silica nanoparticles on the membrane surface, combining the fluoro-containing resin to enhance the adhesion and decrease the surface energy. Using light/heavy water as a model, the hydrogen isotopic separating performance of this composite membrane was evaluated in an air gap membrane distillation (AGMD) apparatus. It was shown that the superhydrophobic coating of the membrane can effectively prevent the liquid water penetrating into the membrane, thus providing a pure vapor process in the membrane. Meanwhile, when compared to pure GOM and commercial polymeric membranes, the resultant membranes acquired superior isotopic selectivity in membrane distillation. The best performing membrane contains three layers of nanoparticles, of which the outermost surface was treated with 40 μL (heptadecafluoro-1, 1, 2, 2-tetrahydrodecyl) trimethoxysilane (17-FTMS) and 10 μL methyltrimethoxysilane (MTMOS). A mean separation factor value of 1.151 and a permeation flux of 0.036 kg m−2 h−1 were obtained. In addition, continuous test for up to 90 h showed a stable performance of the composite membrane, without compromising the selectivity and flux of the membrane. This study not only demonstrates the potential of superhydrophobic composite GOM for hydrogen isotopic sieving in membrane distillation, but also provides a facile and generic method for superhydrophobic modification of the hydrophilic membrane.
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