The kinetics of catalytic incineration of styrene over a MnO/Fe2O3 catalyst

研究成果: Article同行評審

41 引文 斯高帕斯(Scopus)

摘要

Catalytic incineration is one of the cost-effective technologies to deal with unwanted volatile organic compounds (VOCs). Catalytic incineration of styrene over a MnO/Fe2O3 catalyst was carried out in a bench scale catalytic incinerator. Three kinetic models, the power-rate law, the Mars and van Krevelen model and the Langmuir-Hinshelwood model were used to analyze the results. A differential reactor design was used for best fit of kinetic models in this study. The results show that the Langmuir-Hinshelwood model may be feasible to describe the catalytic incineration of styrene. This suggests that the chemical adsorption of either O2 molecules or O atoms is important in the process of catalytic incineration of styrene.

原文English
頁(從 - 到)83-93
頁數11
期刊Science of the Total Environment
275
發行號1-3
DOIs
出版狀態Published - 2001 七月 25

All Science Journal Classification (ASJC) codes

  • 環境工程
  • 環境化學
  • 廢物管理和處置
  • 污染

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