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Colloidal fouling of thin film composite and cellulose acetate reverse osmosis membranes.

机译:薄膜复合材料和醋酸纤维素反渗透膜的胶体结垢。

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This dissertation investigates colloidal fouling of reverse osmosis (RO) membranes by aluminum oxide and silica colloids. The membranes investigated include three types of thin film composite membranes and two types of cellulose acetate membranes. The important factors that affect colloidal fouling, namely, particle concentration, solution chemistry, electrokinetic charge of particles and membranes, permeation drag, and surface morphology, are studied in laboratory experiments.; Solution chemistries tested in this research include ionic strength, pH, divalent ions, and natural organic matter. Solution chemistry affects colloidal fouling of RO membranes by changing double layer forces between particles and membranes and between suspended and retained particles. Colloidal fouling occurs in two stages. At the initial fouling stage, particles interact with the clean membrane surface, whereas at the second stage particles deposit onto previously retained particles rather than onto the bare membrane surface. In the solution pH range investigated, deposition of aluminum oxide colloids onto the membrane surface is initially favorable and later becomes unfavorable as particles accumulate on the membrane surface. Because the silica colloids and membranes are negatively charged, deposition of silica is unfavorable throughout the entire fouling process.; A mechanistic explanation for colloidal fouling of RO membranes is proposed based on the ionic strength, permeation drag and electrokinetic charge of colloids and membranes. Several fouling scenarios are analyzed. The general conclusion is that, at high permeation drag, significant permeate flux decline will be observed regardless of solution chemistry, while at low permeation drag, significant permeate flux decline will be observed only when ionic strength is high. No permeate flux decline will be observed when both solution ionic strength and permeation drag are low.; Membrane surface roughness plays an important role in colloidal fouling. The difference in fouling behavior of thin film composite membranes from that of cellulose acetate membranes is primarily attributable to the different roughness of the membrane surfaces. The smooth cellulose acetate membranes exhibit less fouling tendency, whereas the rough thin film composite membranes are conducive to more severe colloidal fouling.
机译:本文研究了氧化铝和二氧化硅胶体对反渗透膜的胶体污染。研究的膜包括三种类型的薄膜复合膜和两种类型的醋酸纤维素膜。在实验室实验中研究了影响胶体结垢的重要因素,即颗粒浓度,溶液化学性质,颗粒和膜的电动电荷,渗透阻力和表面形态。这项研究中测试的溶液化学包括离子强度,pH,二价离子和天然有机物。溶液化学作用通过改变颗粒和膜之间以及悬浮和保留的颗粒之间的双层力来影响RO膜的胶体结垢。胶体结垢分两个阶段发生。在最初的结垢阶段,颗粒与清洁的膜表面相互作用,而在第二阶段,颗粒沉积在先前保留的颗粒上,而不是沉积在裸露的膜表面上。在研究的溶液pH范围内,氧化铝胶体最初沉积在膜表面是有利的,后来由于颗粒在膜表面积聚而变得不利。因为二氧化硅胶体和膜带负电,所以在整个结垢过程中二氧化硅的沉积都是不利的。基于胶体和膜的离子强度,渗透阻力和电动势,提出了反渗透膜胶体结垢的机理解释。分析了几种结垢情况。总的结论是,在高渗透阻力下,无论溶液化学如何,都会观察到明显的渗透通量下降,而在低渗透阻力下,只有当离子强度高时,才能观察到显着的渗透通量下降。当溶液离子强度和渗透阻力都较低时,不会观察到渗透通量下降。膜表面粗糙度在胶体结垢中起重要作用。薄膜复合膜与乙酸纤维素膜的结垢行为的差异主要归因于膜表面的粗糙度不同。光滑的乙酸纤维素膜表现出较小的结垢趋势,而粗糙的薄膜复合膜则有助于更严重的胶体结垢。

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