4.7 Article

Co/Fe and Co/Al layered double oxides ozone catalyst for the deep degradation of aniline: Preparation, characterization and kinetic model

Journal

SCIENCE OF THE TOTAL ENVIRONMENT
Volume 715, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.scitotenv.2020.136982

Keywords

Ozone catalysts; Layered double oxides; Layered double hydroxides intermediate; Aniline degradation; Kinetic model

Funding

  1. National Science and Technology Major Project-Water pollution control and treatment [2018ZX07208-009-06]
  2. Open Fund project of Qingdao University of Technology [QUTSEME201924]
  3. Technology Development Project of Weifang City [2019ZJ1300]
  4. Zhejiang Heze Environmental Tech Shares Co., LTD Technological Foundation [B220170264]

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In this work, Co/Fe and Co/Al layered double oxides (Co/Fe-LDO and Co/Al- LDO)ozone catalysts were obtained from Col re and Co/Al layered double hydroxides intermediates (Co/Fe-LDH and Co/Al-LDH). Firstly, the optimal preparation parameters of the two intermediates were determined, then the morphology and mineralogy microstructure of the derived Co/Fe-LDO and Co/Al- LDO ozone catalysts were systematically studied. Finally, the reaction kinetics of the two ozone catalysts for the deep degradation of aniline wastewater in catalysts/ozone systems were established. The results showed that the optimal preparation conditions were set as pH 12, temperature 60 degrees C, cobalt-iron ratio 3:1 for Co/Fe-LDH intermediate, and pH 12, temperature 70 degrees C, cobalt-aluminum ratio 3:1 for Co/AI-LDH intermediate. During calcination treatment, the dehydration and recrystallization effect impelled LDH intermediate to form LDO catalyst. The derived ozone catalysts Co/Fe-LDO and Co/Al-LDO possess layered structure, and Co species was mainly based on Co3O4 as the main mineral phase of the two ozone catalysts. The addition of catalyst can realize the deep ozonation catalysis of aniline wastewater. The kinetic models established on the aniline oxidized by ozone or catalyst/ozone systems were both fitted the first-order reactions, and the reaction activation energy for COD & and TOC degradation were significantly reduced in catalyst/ozone system. (C) 2020 Elsevier B.V. All rights reserved.

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