Reclamation of sulfate-laden wastewater via a hybrid selective nanofiltration and electrodialysis metathesis process

电渗析 纳滤 土地复垦 废水 化学 过程(计算) 硫酸盐 复分解 废物管理 环境科学 制浆造纸工业 色谱法 环境工程 有机化学 计算机科学 工程类 生物化学 聚合物 考古 聚合 历史 操作系统
作者
Qing-Bai Chen,Pengfei Li,Jianyou Wang,Yanbin Xu,Jinli Zhao
出处
期刊:Journal of environmental chemical engineering [Elsevier]
卷期号:10 (6): 108712-108712 被引量:2
标识
DOI:10.1016/j.jece.2022.108712
摘要

Electrodialysis metathesis (EDM) could be considered as a sustainable method for reclamation of SO 4 2– from wastewater. However, its feasibility is limited by the coexisting Cl – . In this study, for the first time, an integrated process of selective nanofiltration and EDM (SNF/EDM) was proposed to prepare K 2 SO 4 from sulfate-laden wastewater. In SNF unit, concentration of Na 2 SO 4 accompanied by the efficient separation of Cl – and SO 4 2– were realized in a diafiltration mode. A Na 2 SO 4 concentrate stream (53.0 g/L) of 96.7% purity was obtained employing 4/2 of preconcentration factor and 2.0 MPa of operating pressure. Then, the stream was further treated by EDM process to continuously convert Na 2 SO 4 into K 2 SO 4 using KCl as metathesis solution. Under the relatively optimized operating parameters of 0.5 V repeating unit voltage and 1.25 L/h replenishment flowrate, K 2 SO 4 solution (104.5 g/L) with purity of 92.6% was obtained during two-stage EDM with the energy consumption of 0.59 kWh/(kg·K 2 SO 4 ). Finally, K 2 SO 4 powder was obtained by evaporation process and the product purity met the standard of premium grade agricultural K 2 SO 4 based on XRD and composition analysis. This study thus identified an effective way to make high-valued reclamation of sulfate-laden wastewater which contained considerable amounts of Cl – . • SNF/EDM integrated system for recycling SO 4 2– from wastewater was proposed and examined. • Concentration of Na 2 SO 4 accompanied by separation of SO 4 2– and Cl – were realized via SNF diafiltration. • Two-stage EDM were conducted to convert Na 2 SO 4 to K 2 SO 4 and promote closed cycle of residual brine. • K 2 SO 4 solid with purity of 97.4% was obtained by evaporation and crystallization process.
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