Catalytic incineration of ethylene oxide in the packed bed reactor
Само за регистроване кориснике
2006
Чланак у часопису (Објављена верзија)
Метаподаци
Приказ свих података о документуАпстракт
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.
Кључне речи:
Pt/Al2O3 catalyst / ethylene oxide / catalytic oxidation / kinetics / reactor modelИзвор:
Chemical Engineering Journal, 2006, 116, 3, 173-178Издавач:
- Elsevier
DOI: 10.1016/j.cej.2005.11.007
ISSN: 1385-8947
WoS: 000235644200003
Scopus: 2-s2.0-32144442001
Институција/група
IHTMTY - JOUR AU - Arsenijević, Zorana AU - Grbić, Boško AU - Radić, Nenad AU - Grbavčić, Željko PY - 2006 UR - https://cer.ihtm.bg.ac.rs/handle/123456789/263 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 VL - 116 IS - 3 SP - 173 EP - 178 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", volume = "116", number = "3", pages = "173-178", 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 . .