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Leaching behaviour of a galvanic sludge in sulphuric acid and ammoniacal media

机译:电化学污泥在硫酸和氨介质中的浸出行为

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摘要

Leaching studies of a sludge produced by the physico-chemical treatment of astewaters generated by a Ni/Cr plating plant were carried out in both sulphuric acid and ammoniacal media aiming to decide which of them would be the best treatment for this kind of waste material.The dissolution behaviour of some metals (Cu, Ni, Cr and Zn) was studied in order to assure the best metal recovery conditions in subsequent processes by the use of some separation methods such as solvent extraction and precipitation techniques. Therefore, the study here presenteddeals with the first chemical stage of an integrated treatment process. For the sulphuric acid leaching, maximal conversions obtained were 88.6% Cu, 98.0% Ni and 99.2% Zn for the following experimental conditions: a 100 g L−1 acid concentration, a 5:1 liquid-to-solid ratio (L/S),a particle size less than 1 mm, a digestion time of 1 h, a stirring speed of 700 rpm (all at room temperature and under atmospheric pressure).As expected, no selectivity was achieved for the sulphuric acid leaching, despite this option yielding much higher metal ion dissolution when compared with that reached by ammoniacal leaching. The use of this latter medium allowed the extraction of Cu and Ni without Cr species, but rates of conversion were only about 70% for Cu and 50% for Ni, much lower than those obtained for sulphuric acid leaching.
机译:在硫酸和氨气介质中,对通过镍/铬电镀厂产生的废水进行物理化学处理而产生的污泥进行了浸出研究,旨在确定哪种污泥是处理此类废料的最佳方法。为了确保通过使用某些分离方法(例如溶剂萃取和沉淀技术)在后续工艺中获得最佳的金属回收条件,研究了某些金属(Cu,Ni,Cr和Zn)的溶解行为。因此,这里的研究提出了综合处理过程的第一个化学阶段。对于硫酸浸出,在以下实验条件下:100 g L-1酸浓度,液固比5:1(L / S),获得的最大转化率是88.6%Cu,98.0%Ni和99.2%Zn。 ),粒径小于1毫米,消解时间为1小时,搅拌速度为700 rpm(均在室温和大气压下)。正如预期的那样,尽管有此选择,硫酸浸出仍未达到选择性与氨浸法相比,可产生更高的金属离子溶解度。后一种介质的使用允许提取不含Cr物种的Cu和Ni,但是Cu的转化率仅为70%,Ni的转化率仅为50%,远低于硫酸浸出所获得的转化率。

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