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首页> 外文期刊>Ecotoxicology and Environmental Safety >Purification of the leaching solution of recycling zinc from the hazardous electric arc furnace dust through an as-bearing jarosite
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Purification of the leaching solution of recycling zinc from the hazardous electric arc furnace dust through an as-bearing jarosite

机译:通过轴承罐式纯化从危险电弧炉灰尘中回收锌的浸出溶液

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Leaching of the hazardous electric arc furnace (EAF) dust containing mainly zinc ferrite and zinc oxide, accompanied by minor concentrations of arsenic compounds, was investigated using sulfuric acid. In order to reach the maximum recovery of zinc, the leaching solution was adjusted to recover both iron and zinc at their maximum possible values. To obtain a high recovery value of zinc and iron, analyzed by AAS, the optimum leaching condition was found to be the temperature of 90 degrees C, the sulfuric acid concentration of 3 M, the particle size of 75 mu m, the S/L ratio of 1:10 g/mL and the leaching time of 2 h. The percentages of the zinc and iron recovery under the optimum condition were ca. 98.6% and 99.1% respectively, which were verified by a confirmation test and were very close to the predicted values of 100% based on the optimized model, obtained through the software. From the thermodynamics' point of view, it has been found that Zn2+ is the predominant species (90%) under the leaching condition applied. Moreover, the predominant species of iron are FeSO4+, FeHSO42+, Fe(SO4)(2-) and Fe3+ in the magnitudes of 65.8%, 25.6%, 4.4% and 4.0%, respectively. According to the kinetic results, the controlling step in the leaching was the chemical reaction at the most of the operating temperatures and times. In order to purify the zinc solution for electrowinning, iron and arsenic were removed through the jarosite formation process as confirmed by the XRD results. The speciation of arsenic in the precipitated jarosite was explored by XPS. Finally, the low concentrations of arsenic (less than 0.1 ppm) and iron (less than 50 ppm) were determined by the ICP analysis.
机译:使用硫酸研究含有主要含有锌铁氧体和氧化锌的危险电弧炉(EAF)灰尘的浸出,伴随着少量砷化合物。为了达到锌的最大回收率,调节浸出溶液以在其最大可能值中恢复铁和锌。为了获得锌和铁的高回收值,通过AA分析,发现最佳的浸出条件是90℃的温度,硫酸浓度为3米,粒径为75μm,s / l 1:10 g / ml的比例和2小时的浸出时间。最佳条件下锌和铁回收率的百分比为CA. 98.6%和99.1%,分别通过确认测试验证,并根据通过软件获得的优化模型非常接近预测值100%。从热力学的角度来看,已经发现Zn2 +是施用浸出条件下的主要物种(90%)。此外,铁的主要物种是FeSO4 +,FeHSO 42 +,Fe(SO 4)和Fe3 +分别为65.8%,25.6%,4.4%和4.0%。根据动力学结果,浸出中的控制步骤是在大多数工作温度和时间的化学反应。为了净化用于电烙锌的锌溶液,通过通过XRD结果证实的jAR型形成方法除去铁和砷。 XPS探讨了沉淀的罐装中砷的形状。最后,通过ICP分析确定了低浓度的砷(小于0.1ppm)和铁(小于50ppm)。

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