聚合物负载对超疏水性PVDF/TiO2负载膜蒸馏的影响

N. Hamzah, C. P. Leo, B. .. Ooi
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引用次数: 2

摘要

膜蒸馏(MD)是一种很有吸引力的分离方法,因为它可以回收几乎100%无挥发性的水。MD还被认为是环保的,因为低温废热或太阳能热可以用于分离。尽管MD具有这些强大的功能,但迄今为止并没有广泛用于商业目的。阻碍因素包括缺乏针对MD定制的市售膜,低渗透通量以及操作问题,特别是膜润湿和结垢。在本研究中,采用疏水硅烷对含有TiO2纳米粒子的聚偏氟乙烯(PVDF)膜进行了改性,以提高渗透通量并减少膜润湿。在13 - 16 wt%的负载范围内,通过双浴混凝在编织支架上形成薄膜。该工艺制备的膜具有海绵状结构,表面粗糙。采用低表面能硅烷-三氟-1,1,2,2-四氢辛基三乙氧基硅烷对干膜进行了改性。二氧化钛纳米颗粒包埋在膜上,为硅烷改性过程提供了活性位点。所有膜都具有超疏水表面,水接触角大于160°。聚合物负载的增加使平均孔径从0.41±0.01µm (13 wt%)减小到0.34±0.04µm (16 wt%)。此外,随着掺杂量的增加,膜的孔隙率降低,膜的厚度增加。经过8 h的MD操作,改性PVDF/TiO2膜的渗透通量最高,掺杂率为13wt %。大孔径、高孔隙率、低厚度和高疏水性的膜是一种很有吸引力的分离方法,因为它可以以接近100%的无挥发性截留率回收水。MD还被认为是环保的,因为低温废热或太阳能热可以用于分离。尽管MD具有这些强大的功能,但迄今为止并没有广泛用于商业目的。阻碍因素包括缺乏针对MD定制的市售膜,低渗透通量以及操作问题,特别是膜润湿和结垢。在本研究中,采用疏水硅烷对含有TiO2纳米粒子的聚偏氟乙烯(PVDF)膜进行了改性,以提高渗透通量并减少膜润湿。在13 - 16 wt%的负载范围内,通过双浴混凝在编织支架上形成薄膜。该工艺制备的膜具有海绵状结构,表面粗糙。对干膜进行了改性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effect of polymer loading on superhydrophobic PVDF/TiO2 supported membrane for membrane distillation
Membrane distillation (MD) is an attractive separation process since it can be used to recover water with nearly 100 % non-volatile rejection. MD is also considered to be environmentally friendly since the waste heat at low temperature or the solar energy heat can be used for the separation. Despite of having these great features, MD has not been widely used for commercial purpose up to date. The hindrance factors include the lack of commercially available membrane that tailored for MD, the low permeation flux as well as operational issues especially membrane wetting and fouling. In this work, polyvinylidene fluoride (PVDF) membranes incorporated with TiO2 nanoparticles were modified using hydrophobic silane to enhance the permeate flux and to reduce membrane wetting. The polymer loading was varied in the range of 13 – 16 wt% to form thin membranes on woven support via dual bath coagulation. This coagulation technique produced membranes with spongy structure and rough surface. The dry membrane was modified by using low surface energy silane, tridecafluro-1,1,2,2-tetrahydrooctyl triethoxysilane. TiO2 nanoparticles embedded on membranes provided the active site for silane modification process. All the membranes possess superhydrophobic surface with water contact angle beyond 160 °. The increment of polymer loading reduced the average pore size from 0.41±0.01 µm (13 wt%) to 0.34 ± 0.04 µm (16 wt%). Aside from that, the membrane porosity was reduced while membrane thickness was increased with the increasing polymer loading in dope solution. After 8 h of MD operation, the modified PVDF/TiO2 membrane with 13 wt% polymer loading in dope solution showed the highest permeation flux. The membrane with large pore size, high porosity, low thickness and great hydrophobicity is preferable in MD.Membrane distillation (MD) is an attractive separation process since it can be used to recover water with nearly 100 % non-volatile rejection. MD is also considered to be environmentally friendly since the waste heat at low temperature or the solar energy heat can be used for the separation. Despite of having these great features, MD has not been widely used for commercial purpose up to date. The hindrance factors include the lack of commercially available membrane that tailored for MD, the low permeation flux as well as operational issues especially membrane wetting and fouling. In this work, polyvinylidene fluoride (PVDF) membranes incorporated with TiO2 nanoparticles were modified using hydrophobic silane to enhance the permeate flux and to reduce membrane wetting. The polymer loading was varied in the range of 13 – 16 wt% to form thin membranes on woven support via dual bath coagulation. This coagulation technique produced membranes with spongy structure and rough surface. The dry membrane was modifie...
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