A novel method for nickel recovery and phosphorus removal from spent electroless nickel-plating solution

被引:33
作者
Li, Liuyun [1 ]
Takahashi, Naoki [2 ]
Kaneko, Keiichi [2 ]
Shimizu, Tadaaki [1 ]
Takarada, Takayuki [2 ]
机构
[1] Niigata Univ, Dept Chem & Chem Engn, Niigata 9502181, Japan
[2] Gunma Univ, Fac Sci & Technol, Div Environm Engn Sci, Kiryu, Gunma 3768515, Japan
关键词
Electroless nickel-plating solution; Nickel recovery; Phosphorus removal; Ion exchange; Calcium precipitation; INDUSTRIAL-WASTES; AQUEOUS-SOLUTION; WATER; SEPARATION; PHOSPHATE; ION;
D O I
10.1016/j.seppur.2015.04.029
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A new approach to nickel recovery from spent electroless nickel-plating (ENP) solution was investigated using ion-exchange method with brown coal. Nickel ion-exchange was influenced by the solution pH, with the optimum values of pH 9.0-10.0, and was hindered by the anion species existing in the spent solution, especially for the high concentrations of phosphorus compounds. Calcium hydroxide precipitated most of the phosphorus from spent ENP solution, with the highest phosphorus removal efficiency of 98.2%. At the same time, pH control is required to prevent the co-precipitation of nickel hydroxide. Phosphorus removal with CaCO3 and CaCl2 showed strong pH dependence. The solution pH dropped with CaCl2 addition. As a result, the formation of calcium sulphate occurred prior to that of P-Ca compounds. In contrast, CO32- anions from CaCO3 dissolution reacted with the H+ ions to neutralize the solution and decrease CaCO3 solubility at last, the phosphorus removal reached its maximum of 51%. Combined use of calcium carbonate and calcium chloride improved phosphorus removal, maximizing the phosphorus removal efficiency at 94.8%, and enabling 62% of nickel in the ENP solution to be ion-exchanged into brown coal. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:237 / 244
页数:8
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