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DC Field | Value | Language |
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dc.contributor.author | Romanovskaia, Elena | - |
dc.contributor.author | Romanovski, Valentin | - |
dc.contributor.author | Kwapinski, Witold | - |
dc.contributor.author | Kurilo, Irina | - |
dc.date.accessioned | 2021-04-22T06:10:25Z | - |
dc.date.available | 2021-04-22T06:10:25Z | - |
dc.date.issued | 2021 | - |
dc.identifier.citation | Selective recovery of vanadium pentoxide from spent catalysts of sulfuric acid production: Sustainable approach / Elena Romanovskaia [et al.] // Hydrometallurgy. - 2021. - T. 200. - № 105568 | ru |
dc.identifier.uri | https://elib.belstu.by/handle/123456789/40288 | - |
dc.description | Spent vanadium catalysts of sulfuric acid production (main elemental composition in wt%: 7.5 V, 9.1 K, 10.2 S, 23.2 Si and 1.4 Fe) can be used as a secondary source of vanadium. Extraction of vanadium was studied using two-step leaching (acidic and reductive) of spent vanadium catalysts with further oxidizing of leaching solutions. The factors leaching and hydrolysis temperature, concentration of leaching (H[2]SO[4], Na[2]SO[3]) and oxidizing ((NH[4])[2]S[2]O[8]) reagents, solid/liquid ratio, mixing parameters, and time of leaching and thermohydrolysis were systematically investigated. The solubility of V[2]O[5] was investigated as a function of temperature, pH of sulfuric acid solutions, and concentration of Na[2]SO[3]. The kinetics of V[2]O[5] solubility and reduction were also studied. The vanadium leaching yield after a two-step recovery was 98 wt% after acidic (H[2]SO[4], pH 1.2–1.3) leaching with ultrasonic treatment for 5 min at ambient temperature, followed by reductive leaching in 0.01 Mol/L Na[2]SO[3] solution for 15 min at ambient temperature. The highest vanadium extraction yield from leaching solutions was 98 wt% obtained through oxidizing of leaching solutions by 30 wt%. (NH[4])[2]S[2]O[8] with a molar ratio n(V[2]O[5])/n ((NH[4])[2]S[2]O[8]) of 5/1 for a reaction time of 5 min at 80–90 ◦C. the extracted vanadium product was V[2]O[5] with a purity of 85–87 wt%. The technological scheme has been developed to recycle all obtained products and subproducts. | ru |
dc.format.mimetype | application/pdf | ru |
dc.language.iso | en | ru |
dc.subject | Spent vanadium catalysts | ru |
dc.subject | Extraction of vanadium | ru |
dc.subject | leaching | ru |
dc.subject | hydrolysis | ru |
dc.subject | vanadium oxide | ru |
dc.subject | solubility | ru |
dc.subject | leaching solutions | ru |
dc.subject | waste recycling | ru |
dc.subject | оксид ванадия | ru |
dc.subject | отработанные ванадиевые катализаторы | ru |
dc.subject | извлечение ванадия | ru |
dc.subject | выщелачивание | ru |
dc.subject | окисление | ru |
dc.subject | гидролиз | ru |
dc.subject | растворимость | ru |
dc.subject | рециклинг отходов | ru |
dc.title | Selective recovery of vanadium pentoxide from spent catalysts of sulfuric acid production: Sustainable approach | ru |
dc.type | Article | ru |
dc.identifier.udc | 661.888.1 | - |
dc.identifier.DOI | https://doi.org/10.1016/j.hydromet.2021.105568 | - |
Appears in Collections: | Статьи в зарубежных изданиях |
Files in This Item:
File | Description | Size | Format | |
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Romanovskaia. Selective.pdf | 2.53 MB | Adobe PDF | View/Open |
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