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首页> 外文期刊>Chemosphere >Removal of toxic ions (chromate, arsenate, and perchlorate) using reverse osmosis, nanofiltration, and ultrafiltration membranes
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Removal of toxic ions (chromate, arsenate, and perchlorate) using reverse osmosis, nanofiltration, and ultrafiltration membranes

机译:使用反渗透,纳滤和超滤膜去除有毒离子(铬酸根,砷酸根和高氯酸根)

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摘要

Rejection characteristics of chromate, arsenate, and perchlorate were examined for one reverse osmosis (RO, LFC-1), two nanofiltration (NF, ESNA, and MX07), and one ultrafiltration (UF and GM) membranes that are commercially available. A bench-scale cross-flow flat-sheet filtration system was employed to determine the toxic ion rejection and the membrane flux. Both model and natural waters were used to prepare chromate, arsenate, and perchlorate solutions (approximately 100 μg L~(-1) for each anion) in mixtures in the presence of other salts (KC1, K_2SO_4, and CaCl_2); and at varying pH conditions (4,6, 8, and 10) and solution conductivities (30, 60, and 115 mS m~(-1)). The rejection of target ions by the membranes increases with increasing solution pH due to the increasingly negative membrane charge with synthetic model waters. Cr(VI), As(V), and ClO_4~- rejection follows the order LFC-1 (>90%) > MX07 (25-95%) ≌ ESNA (30-90%) > GM (3-47%) at all pH conditions. In contrast, the rejection of target ions by the membranes decreases with increasing solution conductivity due to the decreasingly negative membrane charge. Cr(Vl), As(V), and ClO_4~- rejection follows the order CaCl_2 < KCI ≌ K_2SO_4 at constant pH and conductivity conditions for the NF and UF membranes tested. For natural waters the LFC-1 RO membrane with a small pore size (0.34 nm) had a significantly greater rejection for those target anions (>90%) excluding NO_3~-(71-74%) than the ESNA NF membrane (11-56%) with a relatively large pore size (0.44 nm), indicating that size exclusion is at least partially responsible for the rejection. The ratio of solute radius (r_(i,s)) to effective membrane pore radius (r_p) was employed to compare ion rejection. For all of the ions, the rejection is higher than 70% when the r_(i,s)/r_p ratio is greater than 0.4 for the LFC-1 membrane, while for di-valent ions (CrO_4~(2-), SO_4~(2-), and HASSO_4~(2-)) the rejection (38-56%) is fairly proportional to the r_(i,s)/r_p ratio (0.32-0.62) for the ESNA membrane.
机译:检查了铬酸盐,砷酸盐和高氯酸盐的排斥特性,其中有一种反渗透膜(RO,LFC-1),两种纳滤膜(NF,ESNA和MX07)和一种超滤膜(UF和GM),它们在市场上都可以买到。使用台式横流平板过滤系统来确定有毒离子排斥和膜通量。在其他盐(KC1,K_2SO_4和CaCl_2)存在的情况下,使用模型水和天然水在混合物中制备铬酸盐,砷酸盐和高氯酸盐溶液(每个阴离子约100μgL〜(-1));在不同的pH条件(4、6、8和10)和溶液电导率(30、60和115 mS m〜(-1))下进行。膜对目标离子的排斥随着溶液pH值的增加而增加,这是由于合成模型水对膜的负电荷越来越大。 Cr(VI),As(V)和ClO_4〜-的去除率遵循LFC-1(> 90%)> MX07(25-95%)≌ESNA(30-90%)> GM(3-47%)在所有pH条件下。相反,由于负离子膜电荷的减少,随着溶液电导率的增加,膜对目标离子的排斥率降低。对于NF和UF膜,在恒定的pH和电导率条件下,Cr(Vl),As(V)和ClO_4〜-的排阻遵循以下顺序:CaCl_2 90%)的排阻(NO_3〜-(71-74%)除外)比ESNA NF膜(11- 56%的样品具有相对较大的孔径(0.44 nm),表明尺寸排阻至少部分是造成排斥的原因。使用溶质半径(r_(i,s))与有效膜孔半径(r_p)之比来比较离子排斥。对于所有离子,当LFC-1膜的r_(i,s)/ r_p比值大于0.4时,截留率均高于70%,而对于二价离子(CrO_4〜(2-),SO_4 〜(2-)和HASSO_4〜(2-))的排斥率(38-56%)与ESNA膜的r_(i,s)/ r_p比率(0.32-0.62)相当成比例。

著录项

  • 来源
    《Chemosphere》 |2009年第2期|228-235|共8页
  • 作者单位

    Korea Institute of Energy Research, New and Renewable Energy Research Division, 71-2 Jang-Dong, Yuseong-Cu, Daejeon 305-343, South Korea;

    Water Desalination and Reuse Center, King Abdullah University of Science and Technology, Box 55455, Jeddah 21534, Saudi Arabia;

    Samsung Engineering Co., Ltd., R&D Center, 39-3, Sungbok-Dong, Yongin, Cyeonggi-Do 449-844, South Korea;

    Kookmin University, Civil and Environmental Department, Seoul 136-702, South Korea;

    Department of Civil and Environmental Engineering, University of South Carolina, Columbia, SC 29208, USA;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    chromate; arsenate; perchlorate; water treatment; membrane rejection;

    机译:铬酸盐;砷高氯酸盐水处理;膜排斥;

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