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碳热还原/熔融分离废SCR催化剂中有价金属 被引量:5

Carbon thermal reduction/melting separation of valuable metals from spent SCR catalysts
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摘要 在热力学计算的基础上,把废SCR催化剂(钒钛系)与碳、铁和石灰等原料混合后装入直流电弧炉中熔化、还原,用SEM、XRD分析渣/铁两相试样的化学成分与物相,研究废SCR催化剂再回收的基础问题,并探讨其碳热还原/熔融分离行为和机理。结果表明,有价金属回收率随n(碳)/n(氧)、温度和碱度等条件而变。在熔池温度为1650℃的条件下,回收废SCR催化剂中二氧化钛、金属的最佳参数为:n(碳)/n(氧)为1.0、碱度为1.0;在此条件下可实现含钒、钨的铁合金与高钛渣的完全分离,铁、钒、钨和二氧化钛的回收率分别达到99%、97%、92%和93.5%。这对于开发废SCR催化剂的回收再利用技术,实现可持续发展具有重大的现实意义和经济价值。 On the basis of thermodynamics calculate,the spent SCR catalyst(V-Ti)was mixed with C,Fe and CaO and then melted and reduced in a DC arc furnace.The chemical composition and phase of slag/iron samples were analyzed by SEM and XRD.The basic problem of spent SCR catalyst recycling was studied,and the behavior and mechanism of carbon thermal reduction/melting separation were discussed.Results showed that the recovery rate of the valuable metal changed with the amount-of-substance ratio of C to O,temperature and basicity etc..Under the condition of molten pool temperature of 1650℃,the optimal parameters of recycling TiO2/metal from spent SCR catalyst were as follows:n(C)/n(O)=1.0 and basicity was 1.0.This can realize the complete separation of ferroalloy containing V and W and high titanium slag.The recovery of Fe,V,W and TiO2 could reach around 99%,97%,92%and 93.5%,respectively.This is of great practical significance and economic value for the development of spent SCR catalyst recycling technology and the realization of sustainable development.
作者 李朴芳 穆林 王社斌 Li Pufang;Mu Lin;Wang Shebin(College of Material Science and Engineering,Taiyuan University of Technology,Taiyuan 030024,China)
出处 《无机盐工业》 CAS CSCD 北大核心 2020年第1期93-98,共6页 Inorganic Chemicals Industry
基金 北京科技大学钢铁冶金新技术国家重点实验室开放基金(KF18-02)
关键词 废SCR催化剂 碳热还原 渣铁分离 spent SCR catalyst carbothermal reduction slag/iron separation
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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:5
  • 3GB13223-201l,火电厂大气污染物排放标准[S].
  • 4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.
  • 5Alemany L J, Berti F, Busca G, et al. Characterization and composition of commercial V2O5-WO3-TiO2 SCR catalysts [ J ]. Applied Catalysis B: Environmental, 1996, 10 (4): 299-311.
  • 6Kim M H, An T H. A commercial V2O5-WO3/TiO2 catalyst used at an NH3-SCR deNOx process in an oil-fired power plant: cause of an increase in deNOxing and NH3 oxidation performances at low temperatures//13th Korean- Japan Symposium on Catalysis [C]. Springer, 2011.
  • 7Xu H, Yan Z Y, Xu X, et al. Experiment study of the pilot ammonia SCR system in a coal-fired power plant//2011 Asia-Pacific Power and Energy Engineering Conference [C]. IEEE, 2011.
  • 8Khodayari R, Odenbrand C U I. Regeneration of commercial TiO2-VzOs-WO3 SCR catalysts used in biofuel plants [J]. Applied Catalysis B : Environmental, 2001, 30 (1/2): 87-99.
  • 9Chen J P, Yang R T. Mechanism of poisoning of the V2O5/ TiO2 catalyst for the reduction of NO by NH3 [J]. Journal of Catalysis, 1990, 125 (2): 411-420.
  • 10Alemany L J, Lietti L, Ferlazzo N, et al. Reactivity and physicochemical characterization of V2O5-WO3/TiO2 de- NOx catalysts [J]. Journal of Catalysis, 1995, 155 (1): 117-130.

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