使用插有活性炭的天然红土固定床色谱柱去除砷(Ⅲ):解决堵塞问题,实现更佳性能

Régie Dimanche Ouedraogo, Corneille Bakouan, A. K. Sakira, B. Sorgho, B. Guel, T. I. Somé, Anne-Lise Hantson, É. Ziemons, D. Mertens, Philippe Hubert, Jean-Michel Kauffmann
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引用次数: 0

摘要

使用夹有两种层(惰性材料,如细砂和砾石,以及吸附材料,如由埃及白兰地制备的活性炭(BA-AC))的天然红土固定床柱去除水溶液中的砷(III)。为了解决水在天然红土固定床柱中渗流时出现的柱堵塞问题,进行了相关研究。实验测试评估了几种固定床柱配置的水力传导性以及各种参数(如粒度、床层高度和初始 As(III)浓度)的影响。渗透率数据表明,在所研究的不同类型的固定床柱中,就性能和成本而言,填充有重复层的红土和活性炭的柱子比其他柱子(即非交错红土;非交错活性炭;重复层的红土和细沙;重复层的红土和砾石)更适合吸附 As(III)。为确定最有效的塔,利用突破曲线进行了一项研究。随着床层高度从 20 厘米增加到 40 厘米,突破时间从 15 小时增加到 85 小时;随着初始 As(III)浓度从 0.5 毫克/升增加到 2 毫克/升,突破时间从 247 小时减少到 32 小时。Bohart-Adams 模型的结果表明,床层高度增加会导致 kAB 和 N0 值下降。利用床层深度服务时间(BDST)模型确定的去除 As(III)的临界床层深度分别为 15.23 厘米和 7.98 厘米,突破率分别为 1%和 20%。结果表明,基于红土层与 BA-AC 交替层的新型低成本吸附多孔系统可用于砷污染水的处理。
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The Removal of As(III) Using a Natural Laterite Fixed-Bed Column Intercalated with Activated Carbon: Solving the Clogging Problem to Achieve Better Performance
Natural laterite fixed-bed columns intercalated with two types of layers (inert materials, such as fine sand and gravel, and adsorbent materials, such as activated carbon prepared from Balanites aegyptiaca (BA-AC)) were used for As(III) removal from an aqueous solution. Investigations were carried out to solve the problem of column clogging, which appears during the percolation of water through a natural laterite fixed-bed column. Experimental tests were conducted to evaluate the hydraulic conductivities of several fixed-bed column configurations and the effects of various parameters, such as the grain size, bed height, and initial As(III) concentration. The permeability data show that, among the different types of fixed-bed columns investigated, the one filled with repeating layers of laterite and activated carbon is more suitable for As(III) adsorption, in terms of performance and cost, than the others (i.e., non-intercalated laterite; non-intercalated activated carbon, repeating layers of laterite and fine sand; and repeating layers of laterite and gravel). A study was carried out to determine the most efficient column using breakthrough curves. The breakthrough increased from 15 to 85 h with an increase in the bed height from 20 to 40 cm and decreased from 247 to 32 h with an increase in the initial As(III) concentration from 0.5 to 2 mg/L. The Bohart–Adams model results show that increasing the bed height induced a decrease in the kAB and N0 values. The critical bed depths determined using the bed depth service time (BDST) model for As(III) removal were 15.23 and 7.98 cm for 1 and 20% breakthroughs, respectively. The results show that the new low-cost adsorptive porous system based on laterite layers with alternating BA-AC layers can be used for the treatment of arsenic-contaminated water.
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