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废SCR脱硝催化剂碱式焙烧—水浸提取钒和钨

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利用碱式焙烧—水浸工艺提取废SCR脱硝催化剂中的钒和钨,以便后续钒和钨的资源化利用.探究了焙烧温度、焙烧时间、Na2CO3 与废催化剂的质量比、水浸温度、水浸时间等对钒和钨浸出效果的影响,结合焙烧产物XRD分析探究其焙烧机理.结果表明,废SCR脱硝催化剂合适的碱式焙烧—水浸条件为:焙烧温度875℃、焙烧时间1.5 h、Na2CO3 与废催化剂的质量比1∶1、水浸温度80℃、水浸时间2 h,在此条件下钒和钨的浸出率分别达到91.33%和96.34%.根据XRD分析结果,在碱式焙烧过程中钒和钨分别转化为易溶性的NaV6O15 和Na2WO4;经过碱式焙烧—水浸处理后,90%以上的钒和钨进入水浸液,而进入水浸液中的钛不足2%.
Extraction of Vanadium and Tungsten from Waste SCR Denitrification Catalyst by Alkaline Roasting and Water Leaching Process
The alkaline roasting and water leaching process was used to extract vanadium and tungsten from the waste SCR denitrification catalyst for the subsequent resource utilization of vanadium and tungsten.The effects of roasting temperature,roasting time,mass ratio of Na2CO3 to waste catalyst,water leaching temperature,and water leaching time on the leaching effect of vanadium and tungsten were investigated.The roasting mechanism was explored by XRD analysis of roasting products.The experimental results show that the suitable alkaline roasting and water leaching conditions for the waste SCR denitrification catalyst include roasting temperature 875℃,roasting time 1.5 hours,mass ratio of Na2CO3 to waste catalyst 1∶1,water leaching temperature 80℃,and water leaching time 2 h.Under these conditions,the leaching rate of vanadium and tungsten is 91.33%and 96.34%respectively.According to the results of XRD analysis,vanadium and tungsten are converted into easily soluble NaV6O15 and Na2WO4 respectively during the alkaline roasting process.After alkaline roasting and water leaching treatment,more than 90%of vanadium and tungsten enters the water leaching solution,while less than 2%of titanium enters the water leaching solution.

waste SCR denitrification catalystalkaline roastingwater leachingvanadiumtungstenleaching rate

俞子铉、李奇勇、李强、刘云龙、罗微、陈茜

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福州大学 化工学院,福州 350108

三明学院 资源与化工学院,福建 三明 365004

清洁生产技术福建省高校工程研究中心,福建 三明 365004

废SCR脱硝催化剂 碱式焙烧 水浸 浸出率

2025

有色金属(冶炼部分)
北京矿冶研究总院

有色金属(冶炼部分)

北大核心
影响因子:1.344
ISSN:1007-7545
年,卷(期):2025.(2)