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首页> 外文期刊>Journal of Environmental Management >Build-up of a continuous flow pre-coated dynamic membrane filter to treat diluted textile wastewater and identify its dynamic membrane fouling
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Build-up of a continuous flow pre-coated dynamic membrane filter to treat diluted textile wastewater and identify its dynamic membrane fouling

机译:建立连续流预涂层动态膜过滤器,以处理稀释的纺织废水并确定其动态膜结垢

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摘要

This research built up a continuous dynamic flow filter membrane to treat diluted textile wastewater and basically investigated dynamic membrane fouling mechanism. By pre-depositing particles activated carbon (PAC) on membrane support material (MSM), a thin layer was formed on its surface, which showed excellent results in removing organic pollutants from diluted textile wastewater. Experimental data were regressed by the Langmuir, Freundlich, Temkin, Dubinin-Radushkevich (D-R) and Sips isotherm models. The three two-parameter isotherms (Temkin, D-R and Freundlich) were the models that best fitted, with respectively 0.977, 0.975 and 0.973 regression coefficients. D-R model has registered the maximum calculated adsorption capacity Q(md,)(cal)(.) = 45.499 mg/g and the mean energy which was required to adsorb 1 mol of MB dye by the DM layer E = 4.249 kJ/mol; indicating the energy distribution onto heterogeneous surface of a physical adsorption process. Furthermore, kinetic models results showed that MB adsorption onto PAC at different initial concentrations follows the pseudo-second order. The obtained results also indicated that a flexible DM layer with different thickness can be formed from different amount of PAC pre-deposited on MSMs, which demonstrated that it was convenient to adjust the required DM thickness to filtrate a known initial concentration for >99% organic pollutants removal efficiency rate. However, DM fouling occurred on small pores MSMs; which resulted in an increase of the filtration pressure what have affected the filtration performance. PAC and MSMs surface morphology and texture structure, before and after filtration, were visualized respectively by Field Emission Scanning Electron Microscopy (FESEM), Fourier Transform Infra-Red and Attenuated Total Reflectance (FTIR/ATR). From these experimental results, a sustainable flux (>6.85 x 10(-5) m/s) was established to discriminate no fouling from fouling conditions based on flux and TMP trends variance.
机译:本研究建立了一种连续的动态流滤膜来处理稀释的纺织废水,并基本研究了动态膜结垢的机理。通过在膜载体材料(MSM)上预沉积颗粒活性炭(PAC),在其表面上形成了一层薄层,这在从稀释的纺织废水中去除有机污染物方面显示出优异的效果。实验数据通过Langmuir,Freundlich,Temkin,Dubinin-Radushkevich(D-R)和Sips等温线模型回归。最好的模型是三个两个参数的等温线(Temkin,D-R和Freundlich),回归系数分别为0.977、0.975和0.973。 D-R模型记录的最大计算吸附容量Q(md,)(cal)(。)= 45.499 mg / g,DM层E吸附1 mol MB染料所需的平均能量= 4.249 kJ / mol;表示能量分布在物理吸附过程的非均质表面上。此外,动力学模型结果表明,在不同的初始浓度下,MB吸附在PAC上的时间都接近假二级。获得的结果还表明,可以通过预先沉积在MSM上的不同数量的PAC来形成具有不同厚度的柔性DM层,这表明可以方便地调整所需的DM厚度,以过滤已知初始浓度的> 99%的有机物。污染物去除效率。但是,DM结垢发生在小孔MSM上。导致过滤压力升高,从而影响了过滤性能。分别通过场发射扫描电子显微镜(FESEM),傅立叶变换红外和衰减全反射(FTIR / ATR)可视化过滤前后的PAC和MSMs表面形态和纹理结构。从这些实验结果中,建立了可持续通量(> 6.85 x 10(-5)m / s),以根据通量和TMP趋势方差将积垢条件与积垢情况区分开。

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