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Effect of flux and feedwater composition on fouling of reverse osmosis and nanofiltration membranes by humic acid.

机译:通量和给水组成对腐殖酸对反渗透膜和纳滤膜的污染作用。

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摘要

Membrane fouling by natural organic matter (NOM) is one of the major problems in membrane filtration. Fouling of reverse osmosis (RO) and nanofiltration (NF) membranes by purified AldrichRTM humic acid (PAHA), a model NOM foulant, was systematically investigated by performing bench-scale fouling tests under constant pressure. Severe flux reduction and foulant accumulation occurred at high initial flux, [H+], and [Ca2+]. High flux promoted fouling probably through increased hydrodynamic drag and concentration polarization. On the other hand, flux was severely affected at low pH and high calcium concentration probably due to reduced electrostatic repulsion between foul ant-membrane and foulant-deposited-foulant.; Transmission electron micrographs of fouled membranes show that membrane coupons, except those with very low initial flux, were completely covered by a layer of humic acid whose thickness and density were greatly affected by feedwater composition ([H+] and [Ca2+]) and initial flux. A low density humic layer (about 0.1 g PAHA/cm 3) was formed at low initial flux (2 m/day or less) at pH 7 without calcium. It was several times denser at higher initial flux, pH 4.5, or 1 mM Ca2+. The denser foulant layers together with the greater PAHA accumulations were responsible for the severe flux reductions at high initial flux, [H+], and [Ca2+]. Streaming potential measurements show that the zeta potential of the fouled membranes was controlled by the humic acid layer due to its complete coverage on the membrane surfaces.; For high initial flux and severe fouling conditions (high [H+ ], [Ca2+], and ionic strength), membrane flux decreased to a limiting value that was independent of membrane properties and the initial flux. Flux reduction was much milder when the initial flux was lower than the limiting flux. The limiting flux was independent of membrane properties, probably due to the dominance of foul ant-deposited-foul ant interaction upon complete foulant coverage over membrane surfaces. On the other hand, the limiting flux depended strongly on the feedwater composition. The limiting flux was reduced at higher proton, calcium, and background electrolytes concentrations, likely due to reduced electrostatic repulsion under these conditions.
机译:天然有机物(NOM)造成的膜污染是膜过滤的主要问题之一。通过在恒压下进行台式规模的结垢测试,系统地研究了纯净的AldrichRTM腐殖酸(PAHA)(一种NOM结垢剂)对反渗透(RO)和纳滤(NF)膜的结垢情况。在高初始通量,[H +]和[Ca2 +]时,发生严重的通量减少和积垢。高通量可能通过增加流体动力阻力和浓度极化来促进结垢。另一方面,在低pH和高钙浓度下,助焊剂受到严重影响,这可能是由于污垢蚁膜和污垢沉积污垢之间的静电排斥力降低所致。污垢膜的透射电子显微照片显示,除初始通量极低的膜片外,膜片完全被腐殖酸层覆盖,腐殖酸的厚度和密度受给水成分([H +]和[Ca2 +])和初始通量的影响很大。在没有钙的情况下,以低初始通量(2 m / day或更小)形成低密度腐殖质层(约0.1 g PAHA / cm 3)。在较高的初始通量,pH 4.5或1 mM Ca2 +下,其密度要高出几倍。较高的初始通量[H +]和[Ca2 +]时,致密的污垢层以及更大的PAHA积累是导致通量严重降低的原因。流电势测量结果表明,由于腐殖酸层完全覆盖了膜表面,因此污垢膜的ζ电势受腐殖酸层控制。对于较高的初始通量和严峻的结垢条件(较高的[H +],[Ca2 +]和离子强度),膜通量降低到一个极限值,该值与膜的性能和初始通量无关。当初始通量低于极限通量时,通量降低要温和得多。极限通量与膜特性无关,这可能是由于在膜表面上完全覆盖污垢后污垢沉积物与污蚁相互作用的优势所致。另一方面,极限通量在很大程度上取决于给水组成。在较高的质子,钙和本底电解质浓度下,极限通量降低,这可能是由于在这些条件下静电排斥力降低所致。

著录项

  • 作者

    Tang, Chuyang.;

  • 作者单位

    Stanford University.;

  • 授予单位 Stanford University.;
  • 学科 Engineering Environmental.
  • 学位 Ph.D.
  • 年度 2007
  • 页码 175 p.
  • 总页数 175
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 环境污染及其防治;
  • 关键词

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