Recovery of nickel, phosphorus and nitrogen from electroless nickel-plating wastewater using bipolar membrane electrodialysis

电渗析 鸟粪石 化学 废水 氮气 电镀(地质) 化学镀镍 核化学 无机化学 化学镀 废物管理 生物化学 有机化学 地球物理学 工程类 地质学 电镀 图层(电子)
作者
Yaoxing Liu,Xiaoyu Wu,Xiaoyun Wu,Liping Dai,Jianguo Ding,Xin Ye,Riyao Chen,Rui Ding,Jianxi Liu,Yanchao Jin,Bart Van der Bruggen
出处
期刊:Journal of Cleaner Production [Elsevier BV]
卷期号:382: 135326-135326 被引量:31
标识
DOI:10.1016/j.jclepro.2022.135326
摘要

Electroless nickel-plating (ENP) wastewater is challenging to treat because of its complex composition. This study used bipolar membrane electrodialysis (BMED) to remove and recover Ni2+, NH4+, total phosphorus (TP) and NO3− from ENP wastewater. The results show that current density significantly affects ion removal and recovery, current efficiency, specific energy consumption and ion migration velocity. When the current density was 20 mA/cm2, the removal ratios of Ni2+, NH4+, TP and NO3− were 100%, 98.6%, 99.3% and 100% after 14 h, respectively, and their recovery ratios were 92.6%, 75.5%, 94.5% and 90.6%, respectively. The removal kinetics analysis showed that the removal of Ni2+, NH4+, TP and NO3− was consistent with the zero-order kinetics process. The current efficiency variated from 42.5% to 39.0% and 37.7%, and the specific energy consumption decreased from 1.67 to 1.38 and 1.32 kW h/mol with the equipped wastewater compartments increased from one to two and three in a BMED system. Post treatment, Ni2+ was recovered as Ni(OH)2, with a purity of 82.6% (commercial Ni(OH)2 purity = 90%). TP was recovered as struvite with a purity of 95.3%, and the physicochemical properties of the obtained struvite were similar to commercial struvite. NH4+ was recovered as (NH4)2SO4 and NH3•H2O. Therefore, BMED is an effective method to recover Ni2+, TP and NH4+ from ENP wastewater.
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