Investigations of catalytic incineration of ethylene oxide (ETO) over Pt/Al2O3 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.
TY - JOUR
AU - Arsenijević, Zorana
AU - Grbić, Boško
AU - Radić, Nenad
AU - Grbavčić, Željko
PY - 2006
UR - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/5424
AB - Investigations of catalytic incineration of ethylene oxide (ETO) over Pt/Al2O3 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.
PB - Elsevier
T2 - Chemical Engineering Journal
T1 - Catalytic incineration of ethylene oxide in the packed bed reactor
EP - 178
IS - 3
SP - 173
VL - 116
DO - 10.1016/j.cej.2005.11.007
ER -
@article{
author = "Arsenijević, Zorana and Grbić, Boško and Radić, Nenad and Grbavčić, Željko",
year = "2006",
abstract = "Investigations of catalytic incineration of ethylene oxide (ETO) over Pt/Al2O3 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.",
publisher = "Elsevier",
journal = "Chemical Engineering Journal",
title = "Catalytic incineration of ethylene oxide in the packed bed reactor",
pages = "178-173",
number = "3",
volume = "116",
doi = "10.1016/j.cej.2005.11.007"
}
Arsenijević, Z., Grbić, B., Radić, N.,& Grbavčić, Ž.. (2006). Catalytic incineration of ethylene oxide in the packed bed reactor. in Chemical Engineering Journal
Elsevier., 116(3), 173-178.
https://doi.org/10.1016/j.cej.2005.11.007
Arsenijević Z, Grbić B, Radić N, Grbavčić Ž. Catalytic incineration of ethylene oxide in the packed bed reactor. in Chemical Engineering Journal. 2006;116(3):173-178.
doi:10.1016/j.cej.2005.11.007 .
Arsenijević, Zorana, Grbić, Boško, Radić, Nenad, Grbavčić, Željko, "Catalytic incineration of ethylene oxide in the packed bed reactor" in Chemical Engineering Journal, 116, no. 3 (2006):173-178,
https://doi.org/10.1016/j.cej.2005.11.007 . .
