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Dye wastewater treatment by direct contact membrane distillation using polyvinylidene fluoride hollow fiber membranes

机译:聚偏二氟乙烯中空纤维膜直接接触膜蒸馏处理染料废水

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The potential of 18 wt.% polyvinylidene fluoride (PVDF) hollow fiber membrane blended with ethylene glycol (EG) for the treatment of dye solution using direct contact membrane distillation (DCMD) system was investigated. The PVDF membrane was prepared using the dry-jet wet spinning method and was characterized in terms of membrane morphology, porosity, wetting pressure, gas permeability and degree of hydrophobicity. The membrane was tested using dye solution containing 0.5 g l(-1) reactive black 5 (RB5). The experimental period was prolonged to 6 h in order to analyze the fouling tendency and membrane durability during the DCMD process. The results showed that the modified PVDF membrane was able to produce consistent flux (i.e., 9.82 +/- 0.52 kg m(-2) h(-1)) throughout the DCMD experiment while maintaining excellent dye rejection (i.e., 99.86 +/- 0.04%). With respect to membrane fouling, it was found that the lumen side of the membrane was significantly stained with color (compared to outer membrane surface) due to the physical-chemical interaction between reactive dye and membrane structure. Although membrane fouling was experienced in this study, its impact on MD performance in terms of flux and rejection was negligible, mainly because MD is not a pressure-driven process.
机译:研究了18 wt。%聚偏二氟乙烯(PVDF)中空纤维膜与乙二醇(EG)混合使用直接接触膜蒸馏(DCMD)系统处理染料溶液的潜力。 PVDF膜使用干喷湿纺法制备,并通过膜形态,孔隙率,润湿压力,透气性和疏水性进行表征。使用含有0.5 g l(-1)反应性黑5(RB5)的染料溶液测试膜。为了分析DCMD过程中的结垢趋势和膜的耐久性,实验时间延长至6小时。结果表明,改性的PVDF膜能够在整个DCMD实验过程中产生一致的通量(即9.82 +/- 0.52 kg m(-2)h(-1)),同时保持出色的染料截留率(即99.86 +/-)。 0.04%)。关于膜结垢,发现由于反应性染料和膜结构之间的物理-化学相互作用,膜的管腔侧被显着地着色(与膜的外表面相比)。尽管在这项研究中经历了膜污染,但是它对通量和截留率对MD性能的影响微不足道,主要是因为MD不是压力驱动的过程。

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