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Preparation of V2O5 using Pb5(VO4)3OH recovered from Bayer vanadium sludge through H2SO4 pre-treatment, H2O2 leaching, V5O12∙6H2O and V10O24∙12H2O precipitation and oxidative roasting at 400 °C
Hydrometallurgy ( IF 4.8 ) Pub Date : 2024-09-19 , DOI: 10.1016/j.hydromet.2024.106404 Changda Zhang, Qiusheng Zhou, Yilin Wang, Leiting Shen, Guihua Liu, Tiangui Qi, Zhihong Peng, Xiaobin Li
Hydrometallurgy ( IF 4.8 ) Pub Date : 2024-09-19 , DOI: 10.1016/j.hydromet.2024.106404 Changda Zhang, Qiusheng Zhou, Yilin Wang, Leiting Shen, Guihua Liu, Tiangui Qi, Zhihong Peng, Xiaobin Li
Bayer vanadium sludge (BVS), discharged during the Bayer alumina production, is a promising secondary resource for the supply of vanadium. Previous vanadium extraction process involving Pb5 (VO4 )3 OH precipitation by PbSO4 , H2 SO4 and (NH4 )2 SO3 leaching, (NH4 )2 S2 O8 oxidation followed by ammonium vanadate precipitation, suffered from large amounts of reagent consumption and discharge of ammonia-containing waste. In this study, a cleaner and cost-efficient process based on H2 SO4 pre-treatment, H2 O2 leaching, hydrolytic precipitation, and preparation of V2 O5 through oxidative roasting was proposed to reduce reagent consumption and waste. Results show that the maximum vanadium leaching efficiency reached 99.7 % under the most suitable conditions of H2 SO4 pre-treatment with H2 SO4 /Pb5 (VO4 )3 OH molar ratio of 6.5, pulp density of 250 g/L at 90 °C for 4 h followed by H2 O2 leaching with H2 O2 /V molar ratio of 3.0 at 15 °C for 10 min. Furthermore, 96.5 % of vanadium was precipitated in the forms of V5 O12 ∙6H2 O and V10 O24 ∙12H2 O by heating the leach liquors to 100 °C for 60 min, followed by the oxidative roasting at 400 °C for 2 h to prepare V2 O5 product with a purity of 99.2 %, with only H2 O as a by-product. This research provides new insights into vanadium extraction in a cleaner, cost-efficient, and sustainable industrial process which saves 147.4 $/t Pb5 (VO4 )3 OH.
中文翻译:
利用拜耳钒油泥中回收的Pb5(VO4)3OH制备V2O5,经H2SO4预处理、H2O2浸出、V5O12∙6H2O和V10O24∙12H2O沉淀和400 °C氧化焙烧
拜耳钒污泥 (BVS) 在拜耳氧化铝生产过程中排放,是一种很有前途的钒供应辅助资源。以前的钒提取过程涉及 PbSO4、H2SO4 和 (NH4)2SO3 浸出 Pb5(VO4)3OH,(NH4)2S2O8 氧化后钒酸铵沉淀,遭受了大量的试剂消耗和含氨废物的排放。在这项研究中,提出了一种基于 H2SO4 预处理、H2O2 浸出、水解沉淀和通过氧化焙烧制备 V2O5 的更清洁且具有成本效益的工艺,以减少试剂消耗和浪费。结果表明,在最适宜的条件下,H2SO4/Pb5(VO4)3OH摩尔比为6.5,纸浆密度为250 g/L,90 °C,4 h,然后H2O2/V摩尔比为3.0,H2O2/V摩尔比为3.0,H2O2在15 °C下浸出10 min,钒浸出效率最高。 将浸出液加热至 100 °C 60 min,然后在 400 °C 下氧化焙烧 2 h,制备纯度为 99.5% 的 V5O12∙6H2O 和 V10O24∙12H2O 的钒,仅以 H2O 为副产品。这项研究为在更清洁、经济高效和可持续的工业过程中提取钒提供了新的见解,可节省 147.4 美元/吨的 Pb5(VO4)3OH。
更新日期:2024-09-19
中文翻译:
利用拜耳钒油泥中回收的Pb5(VO4)3OH制备V2O5,经H2SO4预处理、H2O2浸出、V5O12∙6H2O和V10O24∙12H2O沉淀和400 °C氧化焙烧
拜耳钒污泥 (BVS) 在拜耳氧化铝生产过程中排放,是一种很有前途的钒供应辅助资源。以前的钒提取过程涉及 PbSO4、H2SO4 和 (NH4)2SO3 浸出 Pb5(VO4)3OH,(NH4)2S2O8 氧化后钒酸铵沉淀,遭受了大量的试剂消耗和含氨废物的排放。在这项研究中,提出了一种基于 H2SO4 预处理、H2O2 浸出、水解沉淀和通过氧化焙烧制备 V2O5 的更清洁且具有成本效益的工艺,以减少试剂消耗和浪费。结果表明,在最适宜的条件下,H2SO4/Pb5(VO4)3OH摩尔比为6.5,纸浆密度为250 g/L,90 °C,4 h,然后H2O2/V摩尔比为3.0,H2O2/V摩尔比为3.0,H2O2在15 °C下浸出10 min,钒浸出效率最高。 将浸出液加热至 100 °C 60 min,然后在 400 °C 下氧化焙烧 2 h,制备纯度为 99.5% 的 V5O12∙6H2O 和 V10O24∙12H2O 的钒,仅以 H2O 为副产品。这项研究为在更清洁、经济高效和可持续的工业过程中提取钒提供了新的见解,可节省 147.4 美元/吨的 Pb5(VO4)3OH。