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废脱硝催化剂钒、钨的浸出-搅拌对浸出率的影响 被引量:4

Leaching of V and W fromspent SCR catalyst-Effect of agitation on leaching rates
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摘要 实现废脱硝催化剂高效综合再利用具有重大的社会和经济效益。本文采用NaOH浸出废脱硝催化剂中钒钨离子并考察其浸出影响因素,对比研究了搅拌和不搅拌作用下废脱硝催化剂中的钨离子浸出动力学。结果表明,提高浸出温度和NaOH浓度均有利于钒、钨的浸出;在搅拌条件下(350 r/min),液固比3.5∶1,浸出温度160℃,NaOH浓度40%,浸出时间3.5 h,钒、钨浸出率均达到100%。动力学研究结果钨离子浸出过程属于固膜扩散控制,搅拌条件下钨浸出表观活化能为29.28 kJ/mol,而不搅拌时,其表观活化能仅为1.26 kJ/mol,搅拌强化可增加扩散速率,减小扩散阻力,强化钒钨的浸出。 It is of great economic and social benefits for the recovery and reuse of valuable metals in waste SCR denitrification catalysts.In this paper,the vanadium and tungsten ions in waste denitrification catalyst were leached by NaOH and the factors affecting the leaching rates were investigated.Results showed that increasing the leaching temperature and NaOH concentration were beneficial to the leaching of vanadium and tungsten.The leaching rates of vanadium and tungsten could reach 100%under the condition of liquid-solid ratio of 3.5∶1,leaching temperature of 160℃,NaOH concentration of 40%,and the leaching time of 3.5 h.The process of tungsten ion leaching was controlled by solid membrane diffusion.Under agitation condition(350 r/min),the apparent activation energy of tungsten leaching was 29.28 kJ/mol,while without agitation,the apparent activation energy was only 1.26 kJ/mol.Agitation could increase the diffusion rate,reduce the diffusion resistance,and enhance the leaching rates vanadium and tungsten.
作者 陈洋 金科 陈嘉宇 赵长多 夏启斌 CHEN Yang;JIN Ke;CHEN Jiayu;ZHAO Changduo;XIA Qibin(School of Chemistry and Chemical Engineering, South China University of Technology,Guangzhou 510640, China;Guangdong Energy Group Zhuhai Power Plant, Zhuhai 519000, China)
出处 《功能材料》 EI CAS CSCD 北大核心 2020年第3期3001-3006,共6页 Journal of Functional Materials
基金 广东省科技计划资助项目(2017A020216016) 广州市民生科技攻关计划资助项目(201803030012)
关键词 废SCR催化剂 回收 搅拌 动力学 spent SCR catalyst V W recovery agitation dynamics
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  • 1罗琳,藤田丰久,治进藤.从废弃的钨金属制品中回收钨和钒[J].矿冶,2002,11(1):50-54. 被引量:12
  • 2周涛,刘少光,唐名早,陈成武,徐玉松,吴进明.选择性催化还原脱硝催化剂研究进展[J].硅酸盐学报,2009,37(2):317-324. 被引量:63
  • 3郝喜才,胡斌杰,景中建.酸溶置换法回收废甲醇催化剂中铜锌的研究[J].无机盐工业,2006,38(12):51-53. 被引量:4
  • 4何东升,冯其明,张国范,欧乐明,卢毅屏,邵延海.碱法从石煤中浸出钒试验研究[J].有色金属(冶炼部分),2007(4):15-17. 被引量:33
  • 5李东光,朱萍萍,范雨听,等.废旧金属、电池、催化剂回收利用实例[M].北京:中国电力出版社,2010:205-206.
  • 6Agar. D. W., & Ruppel. W. (1988). Extended reactor concept for dynamic deNOx design. Chemical Engineering Science, 43(8). 2073-2078.
  • 7Angelidis. T. N .. Christoforou. 5 .. Bongiovanni. A .. & Kruse. N. (2002). On the promotion by 502 of the SCR process over Ag/A\z03: Influence of 502 concentration with C3HS versus C3HS as reductant. Applied Catalysis B: Environmental. 39(3). 197-204.
  • 8Arve. 1<., Popov, E. A .. Ronnholm, M .. Klingstedt, F .. Eloranta, j .. Eranen, 1<.. et al. (2004). From a fixed bed Ag-alumina catalyst to a modified reactor design:.
  • 9How to enhance the crucial heterogeneous-homogeneous reactions in HC-SCR. Chemical Engineering Science. 59(22-23), 5277-5282.
  • 10Bonzi, R .. Lietti, L., Castaldi, L.. & Forzatti. P. (2010). NOx removal over a double-bed NSR-SCR reactor configuration. Catalysis Today. 151(3-4),376-385.

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