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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Phosphate adsorption on granular ferric hydroxide to increase product water recovery in reverse osmosis-desalination of secondary effluents
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Phosphate adsorption on granular ferric hydroxide to increase product water recovery in reverse osmosis-desalination of secondary effluents

机译:磷酸盐吸附在颗粒状氢氧化铁上,以提高二级废水的反渗透-淡化中的产品水回收率

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Calcium phosphate precipitation, and in particular calcium hydroxyapatite (HAP)-Ca-5(PO4)(3)OH scaling, is a major factor limiting high recovery in reverse osmosis (RO) of treated effluents. This study evaluated the feasibility of phosphate adsorption in continuous regime on granular ferric hydroxide (GFH) from 2-fold concentrated RO-brines (1st stage of a 2-stage RO desalination train) of secondary effluents. Fixed bed adsorption on granular media was chosen to ensure low turbidity and preserve brine pressure for the 2nd RO stage. Optimal hydraulic conditions for adsorption and a method for GFH regeneration were formulated. Simultaneous analysis of bed mass transfer zone and adsorbent concentration yielded optimum at empty bed contact time (EBCT) > 3.5 min and 10 < hydraulic load (HL) < 15 m/h. Breakthrough P-concentration was set at 0.2 mg/L to maintain HAP-solubility index <= 7. A constant adsorption rate of 1.6 mg P/g GFH was maintained during nine adsorption/ regeneration cycles at feed phosphate concentration of 93 +/- 0.9 ing/L (as P), approx. 3300 bed volumes (BV) per batch. A NaOH regeneration solution was effectively recycled over 2300 BV until reactivation was required. Considering that phosphate concentration in effluents of well performing wastewater treatment plants is far below 10 mg/L, in practice column capacity will be considerable higher than 3300 BV. (C) 2015 Elsevier B.V. All rights reserved.
机译:磷酸钙沉淀,特别是羟基磷灰石钙(HAP)-Ca-5(PO4)(3)OH结垢是限制已处理废水在反渗透(RO)中高回收率的主要因素。这项研究评估了二次浓缩液在二级浓缩RO盐水(2-段RO脱盐系列的第一段)中的颗粒状氢氧化铁(GFH)上连续吸附磷酸盐的可行性。选择在颗粒介质上固定床吸附以确保低浊度并在第二个反渗透阶段保持盐水压力。制定了吸附的最佳水力条件和GFH再生的方法。在空床接触时间(EBCT)> 3.5分钟和10 <水力负载(HL)<15 m / h的情况下,对床传质区和吸附剂浓度的同时分析得到最佳结果。突破性P浓度设置为0.2 mg / L,以保持HAP溶解度指数<=7。在9个吸附/再生循环中,进料磷酸盐浓度为93 +/- 0.9时,恒定吸附率为1.6 mg P / g GFH。 ing / L(以P计),约每批3300床体积(BV)。将NaOH再生溶液有效地循环到2300 BV以上,直到需要重新活化为止。考虑到运行良好的废水处理厂废水中的磷酸盐浓度远低于10 mg / L,实际上,色谱柱容量将大大高于3300 BV。 (C)2015 Elsevier B.V.保留所有权利。

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