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Enhanced fouling and wetting resistance of composite Hyflon AD/poly (vinylidene fluoride) membrane in vacuum membrane distillation

机译:在真空膜蒸馏中增强复合Hyflon Ad / Poly(偏二氟乙烯)膜的污垢和润湿性

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摘要

Membrane fouling and pore wetting are the key problems affecting the separation performance of membrane distillation (MD). They can become more severe with increasing the operation time, which will have a negative impact on heat and mass transfers. In this paper, solutions containing CaCO3, humid acid (HA), and/or silica sols (SiO2) were used as the feed with different Hyflon AD/polyvinylidene fluoride (PVDF) composite membranes for vacuum membrane distillation (VMD). The evolutions of flux and salt rejection during the concentration process were examined, and the membranes with different properties were compared. The results showed that the original membrane was more prone to be fouled and wetted even at low concentration factors. In the single component systems, CaCO3 impacts the membrane performance most severely. With the hybrid component solutions, the flux declines for the composite membranes were lower than that of the original membrane. Compared with the single-component systems, the practical situation is more likely close to the hybrid-component system where fouling and wetting were easier to happen. Overall, the composite membranes showed enhanced fouling and wetting resistance and maintained stable salt rejections. Particularly, the composite membrane with smaller pore sizes (M-40L) performed best among all the membranes, suggesting its high potential for practical VMD applications.
机译:膜污染和毛孔润湿是影响膜蒸馏分离性能(MD)的关键问题。随着越来越多的操作时间,它们可以变得更加严重,这将对热量和质量转移产生负面影响。在本文中,使用含CaCO3,湿酸(HA)和/或二氧化硅溶胶(SiO 2)的溶液用作具有不同Hyflon Ad /聚偏二氟乙烯(PVDF)复合膜的进料,用于真空膜蒸馏(VMD)。检查了浓缩过程中的助熔剂和盐排斥的演变,比较了具有不同性质的膜。结果表明,即使在低浓度因子下,原始膜也更容易被污染和润湿。在单个组件系统中,Caco3最严重地影响膜性能。利用杂交组分溶液,复合膜的通量下降低于原始膜的助熔剂。与单组分系统相比,实际情况更可能接近混合组件系统,其中污垢和润湿更容易发生。总体而言,复合膜显示出增强的污垢和润湿性,保持稳定的盐排斥。特别地,具有较小孔径(M-40L)的复合膜在所有膜中表现最佳,表明其具有实际VMD应用的高潜力。

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  • 作者单位

    Nanjing Tech Univ Coll Chem Engn State Key Lab Mat Oriented Chem Engn Nanjing 210009 Jiangsu Peoples R China;

    Nanjing Tech Univ Coll Chem Engn State Key Lab Mat Oriented Chem Engn Nanjing 210009 Jiangsu Peoples R China;

    Nanjing Tech Univ Coll Chem Engn State Key Lab Mat Oriented Chem Engn Nanjing 210009 Jiangsu Peoples R China;

    Nanjing Tech Univ Coll Chem Engn State Key Lab Mat Oriented Chem Engn Nanjing 210009 Jiangsu Peoples R China;

    Nanjing Tech Univ Coll Chem Engn State Key Lab Mat Oriented Chem Engn Nanjing 210009 Jiangsu Peoples R China;

    Huaiyin Normal Univ Sch Chem &

    Chem Engn Jiangsu Key Lab Chem Low Dimens Mat Huaian 223300 Peoples R China;

    Huaiyin Normal Univ Sch Chem &

    Chem Engn Jiangsu Key Lab Chem Low Dimens Mat Huaian 223300 Peoples R China;

    ITM CNR Res Inst Membrane Technol Via Pietro Bucci 17-C I-87036 Arcavacata Di Rende Italy;

    Nanjing Tech Univ Coll Chem Engn State Key Lab Mat Oriented Chem Engn Nanjing 210009 Jiangsu Peoples R China;

    Macquarie Univ Dept Environm Sci Sydney NSW 2109 Australia;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 分离过程;气化工艺;
  • 关键词

    Membrane fouling; Wetting; Vacuum membrane distillation; Membrane distillation; Composite membrane;

    机译:膜污垢;润湿;真空膜蒸馏;膜蒸馏;复合膜;
  • 入库时间 2022-08-20 05:36:16

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