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首页> 外文期刊>Water, air and soil pollution >Integration of H_2-Based Membrane Biofilm Reactor with RO and NF Membranes for Removal of Chromate and Selenate
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Integration of H_2-Based Membrane Biofilm Reactor with RO and NF Membranes for Removal of Chromate and Selenate

机译:基于H_2的膜生物膜反应器与RO和NF膜的集成,用于去除铬酸盐和硒酸盐

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摘要

A new hybrid process has been proposed and evaluated the feasibility for complete removal of chromate and selenate at high level. The process consists of a H_2-based membrane biofilm reactor (MBfR) and reverse osmosis (RO)anofiltration (NF) stages. The essential feature of the process is the recycling of the RO and NF concentrate into thernmembrane biofilm reactor. First, two different H_2-based denitrifying MBfR initially reduced selenate (Se (Ⅵ)) or chromate (Cr (Ⅲ)) stably to Se° or Cr (Ⅲ) to limited levels (approximately 70-85% removal for selenate and approximately 40-65% removal for chromate). In order to achieve more stable and lower levels, two different membrane (NF and RO) filtration technologies as sequential process were combined. Two wastewaters produced from two MBfRs having similar amounts of target toxic ions (C_o=366 μg-Cr L~(-1) and C_o=326 μg-Se L~(-1)), pH, and conductivity were tested to determine the solute rejection and the membrane flux for one RO and one NF membranes at varying recovery conditions (10-90%). The results show that the rejection of solutes decreases with increasing the recovery due to the increase in osmotic pressure. The rejections by the RO membrane were >99-98% for chromate and 99-94% for selenate, while slightly lower rejections (<20%) were observed for the NF membrane at the recovery conditions.
机译:已经提出了一种新的混合工艺,并评估了完全去除高水平铬酸盐和硒酸盐的可行性。该过程由基于H_2的膜生物膜反应器(MBfR)和反渗透(RO)/纳米过滤(NF)阶段组成。该方法的基本特征是将RO和NF浓缩物再循环到膜生物膜反应器中。首先,两种不同的基于H_2的反硝化MBfR最初将硒酸盐(Se(Ⅵ))或铬酸盐(Cr(Ⅲ))稳定地还原为Se°或Cr(Ⅲ)到有限的水平(硒酸盐的去除率约为70-85%,约40% -65%的铬酸盐去除率)。为了获得更高的稳定性和更低的水平,将两种不同的膜(NF和RO)过滤技术作为顺序过程进行了组合。测试了由两种具有相似目标毒性离子(C_o = 366μg-CrL〜(-1)和C_o = 326μg-SeL〜(-1)),pH和电导率的MBfR产生的两种废水,从而确定了一个RO和一个NF膜在不同的回收率条件下(10-90%)溶质截留率和膜通量。结果表明,由于渗透压的增加,溶质的截留率随着回收率的增加而降低。对于铬酸盐,RO膜的截留率> 99-98%,而硒酸盐的截留率则为99-94%,而在回收条件下,NF膜的截留率略低(<20%)。

著录项

  • 来源
    《Water, air and soil pollution》 |2010年第4期|29-37|共9页
  • 作者单位

    R&D Center, Samsung Engineering Co. Ltd., 415-10 Woncheon-Dong, Youngtong-Gu, Suwon, Gyeonggi-Do 443-823, Republic of Korea;

    Center for Environmental Biotechnology, Biodesign Institute, Arizona State University, 2001 South McAllister Ave, Tempe, AZ 85287-5801, USA;

    Korea Army Academy at Yeong-Cheon, P.O. Box 135-1, Changha-Ri Gogyeong-Myeon, Yeongcheon, Gyeongbuk 770-849, Republic of Korea;

    School of Architectural Engineering, Hongik University, Jochiwon-Eup, Yeonggi-Gun, Chungcheong Nam-Do 339-701, Republic of 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);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    chromate; selenate; hydrogen-based membrane biofilm reactor; reverse osmosis; nanofiltration;

    机译:铬酸盐;硒氢基膜生物膜反应器反渗透;纳滤;

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