کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
4411394 | 1307592 | 2011 | 6 صفحه PDF | دانلود رایگان |

In this study, we examined the experimental catalytic oxidation of gaseous monochlorobenzene (MCBz) with O3 over Fe2O3 in a packed bed reactor to investigate the feasibility of economical low temperature decomposition at a high space velocity (SV). We investigated the effects of several reaction parameters (temperature, O3 concentration, and SV) on the MCBz oxidation. At 150 °C, the conversion of MCBz over Fe2O3 in the absence of O3 was only 3%; it increased to 91% over Fe2O3 in the presence of 1200 ppm of O3 at a high SV of 83 s−1. A long-term operation study revealed that the conversion of MCBz was stable for more than 96 h. In the steady state, the carbon and chlorine balances were 88% and 86%, respectively. Applying a Langmuir–Hinshelwood kinetic model, we estimated an activation energy of 16.7 kJ mol−1 for MCBz oxidation over Fe2O3 in the presence of O3.
Research highlights
► We examine the catalytic oxidation of monochlorobenzene with O3 over Fe2O3.
► Using O3 for the complete oxidation reduces the operating temperature and activation energy.
► No deactivation after 96 h of operation.
► Langmuir–Hinshelwood model can describe the catalytic oxidation of monochlorobenzene.
Journal: Chemosphere - Volume 82, Issue 8, February 2011, Pages 1090–1095