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Recovery of Vanadium and Nickel from a High CaCO3 Containing Petroleum Coke Ash by Roasting and Acidic Leaching
Journal of Sustainable Metallurgy ( IF 2.4 ) Pub Date : 2023-11-08 , DOI: 10.1007/s40831-023-00762-6
Ozgun Yurtseven , Ahmedaljaali Ibrahim Idrees Ibrahim , Soner Top , Sait Kursunoglu , Mahmut Altiner

In this study, it was aimed to extract vanadium (V) and nickel (Ni) from a petroleum coke ash (PCA) using a roasting process without additives, followed by leaching with sulfuric acid (H2SO4). The experiments were designed based on the Taguchi approach, taking into account the parameters of temperature, acid concentration, time, and solid ratio. Additional leaching tests were conducted on the non-roasted PCA for comparison, to assess the effect of roasting on the extractions of V and Ni. The results showed that no extra reducing agent was needed as the PCA contained high levels of CaCO3, which could be used as a reducing agent during roasting. It was found that roasting was essential for high Ni extractions, but had no strong effects on V extractions. The Ni extraction was found to be between 13.3 and 80.8% for the non-roasted PCA and between 43.6 and 99.3% for the roasted PCA. The V extraction was between 36 and 97.9% for the non-roasted PCA and between 45.4 and 99.9% for the roasted PCA. The optimal leaching conditions were determined to be a sulfuric acid of 4.5 M, a solid ratio of 10%, a temperature of 75 °C, and a time of 75 min. In addition, it was determined that the leaching conditions had a great effect on the oxidation state of vanadium ions, and an increase in the acid concentration led to the formation of V3+ ions (green color) instead of VO2+ ions (blue color) in the pregnant leach solution. The final pregnant leach solution containing 1056.50 mg/L V, and 251.85 mg/L Ni was achieved with an extraction yields of > 98%. The experimental results were greatly fitted by the shrinking core model and the activation energy (Ea) for V and Ni was calculated as 3.60 and 4.01 kJ/mol, indicating that the leaching mechanism can be explained by the diffusion control model.

Graphical Abstract



中文翻译:

焙烧酸浸从高碳酸钙石油焦灰中回收钒和镍

在本研究中,目的是使用无添加剂的焙烧工艺从石油焦灰(PCA)中提取钒(V)和镍(Ni),然后用硫酸(H 2 SO 4浸出。实验是基于田口方法设计的,考虑了温度、酸浓度、时间和固体比等参数。对未烘烤的 PCA 进行了额外的浸出测试以进行比较,以评估烘烤对 V 和 Ni 提取的影响。结果表明,不需要额外的还原剂,因为PCA含有高含量的CaCO 3,可以在烘焙过程中用作还原剂。研究发现,焙烧对于高镍提取率至关重要,但对 V 提取率影响不大。未烘烤的 PCA 的 Ni 提取率为 13.3% 至 80.8%,烘烤的 PCA 的 Ni 提取率为 43.6% 至 99.3%。未烘烤的 PCA 的 V 提取率为 36% 至 97.9%,烘烤的 PCA 的 V 提取率为 45.4% 至 99.9%。确定最佳浸出条件为硫酸浓度4.5 M、固形比10%、温度75 ℃、时间75 min。此外,还确定浸出条件对钒离子的氧化态有很大影响,酸浓度的增加导致形成V 3+ 离子绿色)而不是VO 2+离子(蓝色)。颜色)在浸出液中。最终的富浸液含有 1056.50 mg/LV 和 251.85 mg/L Ni,提取率 > 98%。实验结果与缩核模型非常吻合,计算得出V和Ni的活化能(E a )分别为3.60和4.01 kJ/mol,表明浸出机理可以用扩散控制模型来解释。

图形概要

更新日期:2023-11-09
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