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Experimental study on two-stage electrodialysis and reverse osmosis coupling 
process for resource recovery of electroplating industrial wastewater 
Authors: ZHANG Li1, GUO Xiwei2,3, LIU Fang1, LOU Yufeng2,3, FU Rongqiang2,  YANG Sen2, WANG Mengli1
Units: 1. College of Chemical Engineering, Weifang Key Laboratory of High-Salinity Industrial Wastewater 
Resource Utilization, Weifang Vocational College, Weifang 262737, China; 2. Shandong Tianwei 
Membrane Technology Co., Ltd., Weifang 261061, China; 3. Shandong Key Laboratory of Seawater
 Comprehensive Utilization,Shandong Ocean Chemical Industry Scientific Research Institute,
Weifang 262737, China
KeyWords: electrodialysis; reverse osmosis; electroplating industrial wastewater; resource utilization; membrane fouling 
ClassificationCode:TQ028.8
year,volume(issue):pagination: 2026, 46(4):113-127

Abstract:

 Electroplating industrial wastewater features complex compositions and drastic water quality fluctuations. It easily causes scaling and fouling on reverse osmosis (RO) membranes, resulting in deteriorated treatment efficiency and shortened membrane service life. Featuring high separation efficiency and excellent anti-fouling performance, electrodialysis (ED) technology has become a core technical method for advanced resource recovery and zero discharge of complex wastewater. In this study, a two-stage electrodialysis and reverse osmosis coupling process was constructed to realize concentration and volume reduction, advanced desalination and water reuse of electroplating wastewater from a Shaanxi-based enterprise.The experimental results indicated that the first-stage ED unit achieved optimal performance at an operating voltage of 14 V, with an average desalination rate of 91.30%, treatment capacity of 0.251 kg/(m2·h) and desalination energy consumption of 0.514 kW·h/kg. When the second-stage ED unit ran at a current density of 400 A/m2, its average desalination rate reached 88.97%, treatment capacity was 0.561 kg/(m2·h), and desalination energy consumption was 0.245 kW·h/kg. Under an operating pressure of 1.1 MPa and feed flow rate of 160 L/h, the RO unit attained a fresh water recovery rate of 70% and salt rejection rate of 95.93%. The conductivity of effluent water dropped to 43 μS/cm, fully satisfying the reuse standard for makeup water in electroplating workshops.This integrated  process achieved an overall salt removal rate of 99.43%, total water recovery rate of 94.9% and concentration ratio of 19.6, with an annual wastewater treatment power cost of 2.848 million RMB. The system realizes waste salt recycling and water resource reuse. In addition, membrane fouling behaviors and operational stability were systematically analyzed. The research conclusions can provide design guidelines and basic data support for the engineering application of resource-oriented treatment of electroplating industrial wastewater.


Funds:

国家重点研发计划(2022YFB3085104); 山东省重点研发计划(竞争性创新平台)项目(2024CXPT059); 潍坊市科技发展计划(2024ZJ1098, 2025GX055, 2023ZJ1055)


AuthorIntro:
张莉(1980-),女,山东邹城人,副教授,博士,研究方向为高盐工业废水资源化. *通讯作者,E-mail:yf_lou@163.com

Reference:

[1]吴亚东.基于物化生化组合工艺的电镀废水处理分析[J].山西化工,2026,46(2):264-266.
[2]Zhao S F, Lyu F Z, Zhao Y P, et al. Effective strategy for Cr(Ⅵ) removal from water in evolution process of ferroan brucite by redox and intercalation[J]. J Water Process Eng, 2024, 66:105999. 
[3]Erma R, Maji P K, Sarkar S. Detailed investigation of effective trace Cr(Ⅵ) removal mechanism by anion exchange resin with phenolformaldehyde matrix[J]. J Ind Eng Chem, 2022, 111: 147-154.
[4]Zuo Q, Li B, Deng Z Y, et al. Enhanced Cr(Ⅵ) reduction and immobilization by FeO coupled with biochar through galvanic interaction[J]. J Water Process Eng, 2025, 71:107165.
[5]Latifah S A, Nurul A J, Suhaina I, et al. Membrane filtration technologies for sustainable industrial wastewater treatment: a review of heavy metal removal[J]. Desalin Water Treat, 2025, 323:101321.
[6]张艳红,刘伟京,尤本胜,等.用于电镀废水处理的膜技术研究进展[J].膜科学与技术, 2021, 41(4):147-153.
[7]刘兆峰,郭强,唐佳伟,等.二次改性高渗反渗透膜在矿井水脱盐处理中的应用及技术经济性分析[J].煤炭学报,2025,50(S2):1093-1100.
[8]赵丽芳,董健.“电絮凝+反渗透膜”在电镀废水项目的设计与应用[J].膜科学与技术, 2024, 44(5):172-177.
[9]杨毅宁.电渗析在电镀含铬废水零排放中的研究与应用[D].天津:天津工业大学,2023.
[10]季宏飞,李志猛,陈金明,等.电渗析技术在电镀废水零排放方面的应用研究[J].电镀与精饰, 2023, 45(9):64-68.
[11]王玉祺,曹东海,刘蕊,等.氨糖发酵废液的扩散渗析-电渗析耦合脱酸及有机物回收研究[J].膜科学与技术,2026,46(1):140-153.
[12]张莉,康巧能,娄玉峰,等.化妆品废水电渗析脱盐的实验研究[J].盐科学与化工,2022,51(3):12-15,19.
[13]Zhao J, Sun L, Chen Q, et al. Modification of cation exchange membranes with conductive polyaniline for electrodialysis applications[J]. J Membr Sci, 2019, 582:211-223.
[14]Zhang Z R,Luo F B,Jiang C X,et al. Power-free bipolar membrane electrodialysis for acid-alkali production in river estuaries[J]. Chem Eng Sci, 2023, 273:118643.
[15]张玉凤,郭庆,曾娟,等.双极膜电渗析法从含铍碱液中回收碱的研究[J].膜科学与技术,2026,46(1):120-128.
[16]Yang B Q, Ya Y L, Cong T, et al. Sustainable recovery of high-saline papermaking wastewater: Optimized separation for salts and organics via membrane-hybrid process[J]. Desalination, 2021, 507:114938.
[17]董隽,薛上峰,刘春红,等.循环双极膜电渗析处理煤化工含盐废水制备酸碱的研究[J].膜科学与技术,2023,43(2):112-122.
[18]Gao W, Zhao H, Wei X, et al. A green and economical method for preparing potassium glutamate through electrodialysis metathesis[J]. Ind Eng Chem Res, 2022, 61:1486-1493.
[19]Tanaka Y. A computer simulation of feed and bleed ion exchange membrane electrodialysis for desalination of saline water[J]. Desalination, 2010, 254(1/2/3):99-107.
[20]刘颖,董颖波,刘亿鑫,等.双极膜电渗析资源化处理反渗透浓盐水能耗优化[J/OL].工业水处理,1-14[2026-04-06].
[21]Cao R, Xu Y. Efficient preparation of xylonic acid from xylonate fermentation broth by bipolar membrane electrodialysis[J]. Appl Biochem Biotechnol, 2019, 187(1):396-406.
[22]李福勤,陈宇航,郑煚州,等.高盐高COD废水电渗析分盐实验及工程应用[J].水处理技术,2026,52(1):108-112.
[23]刘璐,赵志娟,李雅,等.辛酸对电渗析异相阴离子交换膜污染特性的研究[J].膜科学与技术,2016,36(1):55-60.
[24]中华人民共和国国家市场监督管理总局.均相电渗析膜:GB/T 45010—2024[S].北京:中国标准出版社,2024.
[25]季常青.某矿山冶炼用水脱盐试验研究[J]. 工业水处理, 2025, 45(12):124-128,172.
[26]Mulder M. Basic Principles of Membrane Technology[M].2版.北京:清华大学出版社,1999.


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