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探索高电荷磷酸盐作为正向渗透-膜蒸馏混合系统中的新型汲取剂,用于浓缩高营养污泥。

Exploring high charge of phosphate as new draw solute in a forward osmosis-membrane distillation hybrid system for concentrating high-nutrient sludge.

机构信息

Institute of Environmental Engineering and Management, National Taipei University of Technology, No. 1, Sec. 3, Chung-Hsiao E. Rd, Taipei 106, Taiwan, ROC; Faculty of Environment and Natural Resources, DaLat University, Viet Nam.

Institute of Environmental Engineering and Management, National Taipei University of Technology, No. 1, Sec. 3, Chung-Hsiao E. Rd, Taipei 106, Taiwan, ROC.

出版信息

Sci Total Environ. 2016 Jul 1;557-558:44-50. doi: 10.1016/j.scitotenv.2016.03.025. Epub 2016 Mar 17.

Abstract

For the first time, a high charge of phosphate was used as the draw solute in a forward osmosis-membrane distillation (FO-MD) hybrid system for concentrating high-nutrient sludge. A high water flux (12.5L/m(2)h) and a low reverse salt flux (0.84g/m(2)) were simultaneously achieved at pH9 by using 0.1M Na3PO4 as the draw solute and deionized water as the feed solution in the FO process. The specific reverse salt flux of 0.1M Na3PO4 (Js/Jw=0.07g/L) was considerably less than that of 0.1M NaCl (Js/Jw=0.37g/L) because the complexion between Na(+) and HPO4(2-) at pH9 led to the reduction of free Na(+) ions, which subsequently reduced the reverse salt diffusion substantially. Moreover, for a feed solution with an initial sludge concentration of 3500mg/L, the sludge concentration could be concentrated to 19,800 and 22,000mg/L in the pressure-retarded osmosis (PRO) and FO membrane orientations, respectively, after 15h of operation. Four types of MD membranes were selected for draw solution recovery; of these, a polytetrafluoroethylene membrane with a pore size of 0.45μm was the most effective in achieving a high water flux (10.28L/m(2)h) and high salt rejection (approximately 100%) in a diluted Na3PO4 draw solution.

摘要

首次使用高浓度磷酸盐作为汲取液,在正向渗透-膜蒸馏(FO-MD)混合系统中浓缩高营养污泥。在 pH9 下,使用 0.1M 的 Na3PO4 作为汲取液,去离子水作为进料溶液,FO 过程中实现了高水通量(12.5L/m(2)h)和低反向盐通量(0.84g/m(2))。0.1M 的 Na3PO4 的特定反向盐通量(Js/Jw=0.07g/L)明显小于 0.1M NaCl 的反向盐通量(Js/Jw=0.37g/L),因为在 pH9 下 Na(+)与 HPO4(2-) 的络合导致游离 Na(+)离子减少,从而大大减少了反向盐扩散。此外,对于初始污泥浓度为 3500mg/L 的进料溶液,在 15h 的运行后,PRO 和 FO 膜方向的污泥浓度分别可浓缩至 19800 和 22000mg/L。为了回收汲取液,选择了四种类型的 MD 膜;其中,孔径为 0.45μm 的聚四氟乙烯膜在回收稀释的 Na3PO4 汲取液时,水通量(10.28L/m(2)h)和盐截留率(约 100%)最高。

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