工业水处理 ›› 2023, Vol. 43 ›› Issue (8): 115-122. doi: 10.19965/j.cnki.iwt.2022-0844

• 试验研究 • 上一篇    下一篇

TiOF2纳米催化剂的制备及催化臭氧氧化性能

刘宝亮1(), 于志浩1, 彭倩1, 李东升1, 徐会君2, 杜庆洋1(), 张博明3   

  1. 1. 山东理工大学材料科学与工程学院,山东 淄博 255049
    2. 山东理工大学化学化工学院,山东 淄博 255049
    3. 山东产业技术研究院先进材料学院,山东 济南 250000
  • 收稿日期:2023-05-18 出版日期:2023-08-20 发布日期:2023-08-28
  • 作者简介:

    刘宝亮(1997— ),硕士。E-mail:

    杜庆洋,教授。E-mail:

  • 基金资助:
    山东省自然科学基金面上项目(ZR2019 mEM045)

Preparation of TiOF2 nano-catalyst and its ozone catalytic oxidation performance

Baoliang LIU1(), Zhihao YU1, Qian PENG1, Dongsheng LI1, Huijun XU2, Qingyang DU1(), Boming ZHANG3   

  1. 1. School of Materials Science and Engineering, Shandong University of Technology, Zibo 255049, China
    2. School of Chemistry and Chemical Engineering, Shandong University of Technology, Zibo 255049, China
    3. Institute of Advanced Materials, Shandong Institutes of Industrial Technology, Jinan 250000, China
  • Received:2023-05-18 Online:2023-08-20 Published:2023-08-28

摘要:

以钛酸丁酯、氢氟酸为主要原料,通过水热法制备了纳米TiOF2臭氧氧化催化剂。利用XRD、FT-IR、SEM、XPS对合成的样品进行表征,苯胺作为目标污染物进行催化性能测试。成功制备了球花状TiOF2纳米催化剂,其粒径为180~200 nm,比表面积为105.38 m2/g。碱性环境可以促进反应进行,OH-可以使反应正向进行促进污染物降解,过量的催化剂不利于反应进行,催化剂投加质量浓度高于0.6 g/L时会因团聚导致降解率下降。在催化剂投加质量浓度为0.6 g/L,初始COD为250 mg/L,臭氧流量为0.1 L/min,pH=10时,反应80 min后,降解率达到了98.83%。球花状TiOF2由纳米片拼插形成,这种结构为催化剂提供了复杂的表面,使催化剂具有较大的比表面积,暴露更多的活性位点,为反应提供更多的反应场所。F-使催化剂中生成氧空位和Ti3+,更利于吸附H2O形成表面—OH基团,便于吸附解离水分子从而提供更多的·OH,促进了反应进行,提高了O3的COD降解能力。

关键词: 水处理, 纳米催化剂, 氧空位, 臭氧催化氧化

Abstract:

Nano TiOF2 ozone oxidation catalyst was prepared by hydrothermal method with butyl titanate and hydrofluoric acid as main raw materials. The synthesized samples were characterized by XRD,FT-IR,SEM and XPS,and the catalytic performance was tested with aniline using as the target pollutant. The ball-flower TiOF2 nano-catalyst was successfully prepared,and its particle size was 180-200 nm,and the specific surface area was 105.38 m2/g. The OH- could make the reaction forward to promote the degradation of pollutants in alkaline environment,excessive catalyst was not conducive to the reaction. The catalyst dosage higher than 0.6 g/L would occur agglomeration phenomenon,resulting in degradation rate. When catalyst dosage was 0.6 g/L,initial COD was 250 mg/L,ozone mass concentration was 0.1 L/min,pH=10,the degradation rate reached 98.83% after reacting for 80 min. The ball flower TiOF2 was formed by the splice of nanosheets,this structure provided a complex surface for the catalyst and made the catalyst have a larger specific surface area,exposing more active sites and providing more reaction sites for the reaction. F- could generate oxygen vacancies and Ti3+ in the catalyst,which was more conducive to the adsorption of H2O to form OH groups on the surface and benefit to the adsorption and dissociation of water molecules to provide more ·OH. It promoted the reaction,and improved the COD degradation capacity of O3.

Key words: water treatment, nano-catalyst, oxygen vacancy, ozone catalytic oxidation

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