Catalytic incineration of ethylene oxide in the packed bed reactor
| Autor: | Željko Grbavčić, Boško Grbić, Zorana Arsenijević, Nenad Radić |
|---|---|
| Rok vydání: | 2006 |
| Předmět: |
020209 energy
General Chemical Engineering Kinetics 02 engineering and technology ethylene oxide 7. Clean energy Industrial and Manufacturing Engineering Catalysis Reaction rate chemistry.chemical_compound 0202 electrical engineering electronic engineering information engineering Environmental Chemistry Packed bed Ethylene oxide Waste management General Chemistry 021001 nanoscience & nanotechnology Pt/Al2O3 catalyst Incineration Catalytic oxidation chemistry Chemical engineering kinetics reactor model 0210 nano-technology catalytic oxidation Space velocity |
| Zdroj: | Chemical Engineering Journal |
| ISSN: | 1385-8947 |
| DOI: | 10.1016/j.cej.2005.11.007 |
| Popis: | Investigations of catalytic incineration of ethylene oxide (ETO) over Pt/Al 2O3 catalyst have been conducted on laboratory and pilot scale level. The measurements of the reaction rate conducted under gradientless conditions have been used to evaluate kinetics parameters valuable for reactor modeling. A reactor model is proposed which could a priori predict behavior of catalytic convertor under various operating conditions (inlet temperature, inlet pollutant concentration and space velocity) based on the kinetics parameters and mass and energy balances. The results show satisfactory agreement between predicted and experimental values of conversion and temperature profiles along the catalyst bed. © 2005 Elsevier B.V. All rights reserved. |
| Databáze: | OpenAIRE |
| Externí odkaz: |
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