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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:
采用拜耳钒污泥中回收的 Pb5(VO4)3OH,经 H2SO4 预处理、H2O2 浸出、V5O12∙6H2O 和 V10O24∙12H2O 沉淀以及 400 ℃氧化焙烧制备 V2O5
拜耳氧化铝生产过程中排出的拜耳钒污泥(BVS)是一种很有前景的钒供应二次资源。以往提钒工艺采用PbSO4、H2SO4、(NH4)2SO3浸出沉淀Pb5(VO4)3OH,(NH4)2S2O8氧化,然后沉淀钒酸铵,存在大量试剂消耗和含氨废水排放的问题。本研究提出了一种基于 H2SO4 预处理、H2O2 浸出、水解沉淀和通过氧化焙烧制备 V2O5 的清洁且经济高效的工艺,以减少试剂消耗和浪费。结果表明,在H2SO4/Pb5(VO4)3OH摩尔比为6.5、矿浆密度为250 g/L、90 ℃、4 h的H2SO4预处理最适宜条件下,钒的最大浸出率可达99.7%。 H2O2 浸出,H2O2/V 摩尔比为 3.0,15 °C,浸出 10 分钟。此外,通过将浸出液加热至100°C 60分钟,然后在400°C氧化焙烧2小时,以V5O12·6H2O和V10O24·12H2O的形式沉淀出96.5%的钒,以制备V2O5产品纯度为 99.2%,仅副产物 H2O。这项研究为更清洁、经济高效且可持续的工业流程中提钒提供了新见解,可节省 147.4 美元/吨 Pb5(VO4)3OH。
更新日期:2024-09-19
中文翻译:
采用拜耳钒污泥中回收的 Pb5(VO4)3OH,经 H2SO4 预处理、H2O2 浸出、V5O12∙6H2O 和 V10O24∙12H2O 沉淀以及 400 ℃氧化焙烧制备 V2O5
拜耳氧化铝生产过程中排出的拜耳钒污泥(BVS)是一种很有前景的钒供应二次资源。以往提钒工艺采用PbSO4、H2SO4、(NH4)2SO3浸出沉淀Pb5(VO4)3OH,(NH4)2S2O8氧化,然后沉淀钒酸铵,存在大量试剂消耗和含氨废水排放的问题。本研究提出了一种基于 H2SO4 预处理、H2O2 浸出、水解沉淀和通过氧化焙烧制备 V2O5 的清洁且经济高效的工艺,以减少试剂消耗和浪费。结果表明,在H2SO4/Pb5(VO4)3OH摩尔比为6.5、矿浆密度为250 g/L、90 ℃、4 h的H2SO4预处理最适宜条件下,钒的最大浸出率可达99.7%。 H2O2 浸出,H2O2/V 摩尔比为 3.0,15 °C,浸出 10 分钟。此外,通过将浸出液加热至100°C 60分钟,然后在400°C氧化焙烧2小时,以V5O12·6H2O和V10O24·12H2O的形式沉淀出96.5%的钒,以制备V2O5产品纯度为 99.2%,仅副产物 H2O。这项研究为更清洁、经济高效且可持续的工业流程中提钒提供了新见解,可节省 147.4 美元/吨 Pb5(VO4)3OH。