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Comparison of physico-chemical pretreatment methods to seawater reverse osmosis: Detailed analyses of molecular weight distribution of organic matter in initial stage

机译:理化预处理方法与海水反渗透方法的比较:初期有机物分子量分布的详细分析

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摘要

In desalination, effective pretreatment is the key to reduce membrane fouling that occurs during the seawater reverse osmosis (SWRO) process. However, it is difficult to compare the flux decline after different pretreatments using a small-scale reverse osmosis filtration unit. In this study, we successfully evaluated the effect of pretreatment on SWRO in terms of molecular weight distribution (MWD) of seawater organic matter (SWOM) after 20h of SWRO operation. Microfiltration (MF), ultrafiltration (UF), ferric chloride (FeCl(3)) flocculation and powdered activated carbon (PAC) adsorption, were used as pretreatment. The effluents and the retentates after each pretreatment and 20 h of SWRO operation were characterized in terms of MWD. Although the normalized flux of SWRO showed similar flux decline (J/J(0) = 0.17) with/without pretreatment, SWOM concentration in the retentates after different pretreatments was different in quantity and it increased linearly with time. The slope of the SWOM increase was 0.110, 0.096, 0.077 and 0.059 after MF, FeCl(3) flocculation, UF and PAC adsorption pretreatments, respectively. MW peaks for the seawater used in this study consisted of 1200 Da (biopolymers), 950 Da (fulvic acids), 650 Da (hydrolysates of humic substances), 250 Da (low MW acids) and 90 Da (low MW neutrals and amphiphilics). FeCl(3) flocculation preferentially removed 1200 Da (biopolymers), while PAC adsorption mostly removed 950 Da (fulvic acids). UF and NF removed only a marginal amount of relatively large organics, while RO removed the majority of organics. The intensity of 1200, 950, 650 and 250 Da MW in the RO retentates increased with the RO operation time. The organics of MW around 1200 Da (biopolymers) had a relatively low rate of increase with time compared with those of lower MW. This suggests that the SWOM of 1200 Da MW was preferentially retained on the membrane surface. (C) 2008 Elsevier B.V. All rights reserved
机译:在海水淡化中,有效的预处理是减少海水反渗透(SWRO)过程中发生的膜污染的关键。但是,使用小型反渗透过滤装置比较不同预处理后的通量下降是困难的。在这项研究中,我们成功地进行了SWRO操作20小时后,根据海水有机物(SWOM)的分子量分布(MWD)评估了预处理对SWRO的效果。微滤(MF),超滤(UF),氯化铁(FeCl(3))絮凝和粉末状活性炭(PAC)吸附均用作预处理。每次预处理和SWRO操作20小时后的废水和截留物均根据MWD进行表征。尽管在有/无预处理的情况下,SWRO的归一化通量显示出相似的通量下降(J / J(0)= 0.17),但不同预处理后截留物中的SWOM浓度在数量上有所不同,并且随时间线性增加。 MF,FeCl(3)絮凝,UF和PAC吸附预处理后,SWOM的斜率分别为0.110、0.096、0.077和0.059。本研究中使用的海水的MW峰包括1200 Da(生物聚合物),950 Da(富里酸),650 Da(腐殖质的水解物),250 Da(低MW酸)和90 Da(低MW中性和两亲性)。 。 FeCl(3)絮凝可优先去除1200 Da(生物聚合物),而PAC吸附则最多可去除950 Da(富里夫酸)。 UF和NF仅去除了少量的相对较大的有机物,而RO去除了大部分有机物。 RO截留物中的1200、950、650和250 Da MW的强度随RO操作时间的增加而增加。与较低分子量的有机物相比,分子量约为1200 Da的有机物(生物聚合物)随时间的增长速率相对较低。这表明1200Da MW的SWOM优先保留在膜表面上。 (C)2008 Elsevier B.V.保留所有权利

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