4.7 Article

Hydrometallurgical process development to recycle valuable metals from spent SCR deNOX catalyst

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SCIENTIFIC REPORTS
卷 11, 期 1, 页码 -

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NATURE PORTFOLIO
DOI: 10.1038/s41598-021-01726-0

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  1. R&D Center for Valuable Recycling (Global-Top R&D Program) of the Ministry of Environment, Korea [2019002230001]
  2. Korea Institute of Energy Technology Evaluation and Planning (KETEP) - Korea government(MOTIE) [20217510100020]
  3. Korea Evaluation Institute of Industrial Technology (KEIT) [20217510100020] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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The study compared the soda roasting process of spent SCR catalyst with dissolved NaOH to the usual dry roasting with NaOH, and its impact on subsequent water leaching. By optimizing parameters such as roasting temperature, time, and leaching process, the research achieved a significant reduction in roasting temperature and leaching time, resulting in a high leaching efficiency of vanadium and tungsten while minimizing silicon impurities.
Spent catalyst, containing vanadium and tungsten oxide in a TiO2 glass fiber matrix, pose a risk of environmental contamination due to the high toxicity of its metal oxides if leached into the soil when disposed in landfills. Due to the increasing demand of metals and the continuous depletion of primary resources there is an growing necessity for recycling and reprocessing of spent catalysts and other secondary metal sources for environmental and economical reasons. Study of spent SCR catalyst soda roasting process with dissolved NaOH compared with the usual NaOH dry roasting and its influence in the subsequent water leaching. After optimization, the ideal parameters are roasting using a 0.4 ratio of NaOH/spent SCR catalyst in solution for 2 h at 973 K and de-ionized water leaching for 30 min, at 298 K with a pulp density of 30%. The research results show an important reduction of the roasting temperature and leaching time during the processing of spent SCR catalyst obtaining a 95.4% W and 80.2% V leaching efficiency liquor. Silicon compounds are one of the main impurities leached alongside the valuable metals and in this work, the silicon compounds leached are reduced significantly with the aim of avoiding the de-silication post-processing of the leach liquor. The main advantage of the proposed process is the increase of the leaching efficiency of vanadium and tungsten with a minimization of silicon impurities in a shorter time regardless of the leaching temperature.

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