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Composition and reversibility of fouling on low-pressure membranes in the filtration of coagulated water: insights into organic fractions behaviour

机译:凝固水过滤中低压膜结垢的组成和可逆性:有机级分的见解

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The primary problem for the application of microfiltration (MF) and ultrafiltration (UF) membrane technology is membrane fouling. Such is the case that understanding membrane fouling has become one of the major factors driving MF and UF membrane technology forward. Nevertheless, identifying the constituents that most contribute to membrane fouling and quantifying how they are detached when backwashing (BW) and cleaning-in-place (CIP) are applied still remains a challenging task. The aim of the present study was to quantify membrane fouling development during filtration and membrane fouling detachment during BW and CIP in terms of membrane permeability changes and masses of inorganic and organic constituents accumulated on the membrane. The study was conducted using bench-scale MF and UF modules fed with coagulated and settled water coming from a drinking water treatment plant and operated under dead-end and cross-flow operation modes. The experiments consisted inconsecutive permeation (20min) alternated with BW with permeate water (1.0min) (periodically chemically assisted with NaClO and NaOH) and followed by a two-stage CIP consisting first in an oxidising and basic step (NaClO and NaOH) and second in an acidic step (citric acid). Feed, permeate, retentate (when present) and cleaning discharge streams were monitored for turbidity, total and dissolved organic carbon (TOC and DOC, respectively), UV254 and inorganic ions (Al, Fe, P). DOC was fractionated by high-performance size exclusion chromatography to gain insight into the behaviour of the different organic fractions. Results showed that both MF and UF membranes successfully removed turbidity, Al and Fe, whereas UV254 was moderately removed and TOC and DOC poorly removed, with removal percentages higher for UF than for MF. With regard to the organic fractions, the largest molecular weight compounds were moderately removed while the smallest organic fractions seemed to totally permeate through both membranes. The results also showed that foulants were poorly washed out from the membrane by BW, but better extracted by the two-stage CIP up to a complete detachment for some foulants.
机译:微滤液(MF)和超滤(UF)膜技术应用的主要问题是膜污垢。这种情况是理解膜污垢已成为推动MF和UF膜技术前进的主要因素之一。然而,鉴定最多有助于膜污染和量化它们在反洗(BW)和清洁(CIP)时脱离的组成部分仍然是一个具有挑战性的任务。本研究的目的是在BW和CIP期间量化过滤和膜污垢脱离期间的膜污垢脱落,并在膜渗透性变化和膜上积累的无机和有机成分的质量。该研究是使用从饮用水处理厂的凝固和沉降的凝固和沉降的水中供给的平坦MF和UF模块进行,并在死端和横流操作模式下操作。该实验组成,与渗透水(1.0min)(定期化学辅助NaClO和NaOH)交替的渗透渗透(20mIn)交替,然后进行两级CIP,其首先在氧化和碱性步骤(NaClO和NaOH)中组成。在酸性步骤(柠檬酸)中。对浊度,总和溶解的有机碳(TOC和DOC),UV254和无机离子(Al,Fe,P)进行饲料,渗透物,渗透物(当存在时)和清洁放电流的饲料和清洁放电流。通过高性能尺寸排阻色谱法分离DOC,以了解不同有机级分的行为。结果表明,MF和UF膜成功消除了浊度,Al和Fe,而UV254被激增,TOC和DOC除去差,除去比MF更高。关于有机级分,中度除去最大的分子量化合物,而最小的有机级分似乎完全渗透到两个膜上。结果还表明,由BW的膜从膜中掉出污垢,但通过两级CIP提取更好地提取到一些污垢的完全脱离。

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