高铁酸钾氧化自絮凝处理实际化学镀镍废槽液
Treatment of actual electroless nickel plating bath waste by potassium ferrate oxidation and self-flocculation
（a）过Na柱后Ni的剩余量；（b）投加K2FeO4后Ni去除率；（c）不同pH下废槽液的Ni去除率；（d）不同pH下苹果酸-Ni配水的Ni去除率
高铁酸钾氧化自絮凝处理实际化学镀镍废槽液 |
| 熊秀琴,谢观生,余真,赖玲,邵鹏辉,杨利明,石慧,罗旭彪 |
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Treatment of actual electroless nickel plating bath waste by potassium ferrate oxidation and self-flocculation |
| Xiuqin XIONG,Guansheng XIE,Zhen YU,Ling LAI,Penghui SHAO,Liming YANG,Hui SHI,Xubiao LUO |
| 图5 不同条件下模拟废水和废槽液的Ni去除情况 （a）过Na柱后Ni的剩余量；（b）投加K2FeO4后Ni去除率；（c）不同pH下废槽液的Ni去除率；（d）不同pH下苹果酸-Ni配水的Ni去除率 |
| Fig. 5 Removal of Ni from simulated wastewater and bath waste under different conditions |
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