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Treatment of coastal well water using ultrafiltration-nanofiltration-reverse osmosis to produce isotonic solutions and drinking water: Fouling behavior and energy efficiency

机译:使用超滤-纳滤-反渗透产生等渗溶液和饮用水处理沿海井水:结垢行为和能源效率

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摘要

In the current paper, a suggested process of coupled ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO) to produce isotonic solution (IS) and drinking water from coastal well water was investigated. Due to its high fouling potential, the feed water was pretreated using UF. Results showed that UF eliminates almost the totality of natural organic matter (NOM), and a relatively high portion of calcium (calcium rejection similar to 75%) due to the complex Ca-NOM formed. To understand the fouling mechanism, previously developed mathematical models and equations were adopted. It was shown that the fouling mechanism for UF fits the blocking pores model. For NF, the extended model using cross-flow mode showed a slight difference compared to UF (No compression cake phase). It was concluded that, with some experimental precautions, fouling mechanism of the NF membrane used is internal pore blocking mechanism. Due to its attractive quality, the brine of NF was used to produce drinking water by RO treatment. The energy consumption of the UF-NF-RO system was investigated for different operating conditions. Finally, the permeate of the UF-NF process was compared to a commercialized IS. It was found that the two solutions revealed a remarkable similarity. However, a specific post-treatment should be added to the process to accomplish the pharmaceutical exigencies of IS. (C) 2018 Elsevier Ltd. All rights reserved.
机译:在本文中,研究了一种建议的结合超滤(UF),纳滤(NF)和反渗透(RO)的方法来生产等渗溶液(IS)和沿海井水的饮用水。由于其极高的结垢潜力,使用超滤对进水进行了预处理。结果表明,由于形成了复杂的Ca-NOM,UF几乎消除了全部天然有机物(NOM),并消除了相对较高的钙含量(钙排斥率接近75%)。为了了解结垢机理,采用了以前开发的数学模型和方程式。结果表明,超滤的结垢机理符合阻塞孔模型。对于NF,与UF(无压缩滤饼相)相比,使用错流模式的扩展模型显示出细微的差异。结论是,在一些实验预防措施的基础上,所使用的NF膜的结垢机理是内部孔阻塞机理。由于其吸引人的质量,NF盐水被用于RO处理来生产饮用水。研究了UF-NF-RO系统在不同运行条件下的能耗。最后,将UF-NF工艺的渗透物与商业化的IS进行了比较。发现这两种解决方案显示出显着的相似性。但是,应在过程中添加特定的后处理,以实现IS的药学迫切性。 (C)2018 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Journal of Cleaner Production》 |2018年第1期|1053-1064|共12页
  • 作者单位

    Water Res & Technol Ctr, Lab Nat Water Treatment, Technopk Borj Cedria,BP 273, Soliman 8020, Tunisia;

    King Abdulaziz Univ, Ctr Excellence Desalinat Technol, POB 80200, Jeddah 21589, Saudi Arabia;

    Water Res & Technol Ctr, Lab Water Membrane & Environm Biotechnol, PB 273, Soliman 8020, Tunisia;

    Water Res & Technol Ctr, Lab Nat Water Treatment, Technopk Borj Cedria,BP 273, Soliman 8020, Tunisia;

    Water Res & Technol Ctr, Lab Water Membrane & Environm Biotechnol, PB 273, Soliman 8020, Tunisia;

    Water Res & Technol Ctr, Lab Nat Water Treatment, Technopk Borj Cedria,BP 273, Soliman 8020, Tunisia;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Nanofiltration; Ultrafiltration; Reverse osmosis; Energy consumption; Fouling;

    机译:纳滤;超滤;反渗透;能耗;结垢;

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