Hydrotreating of middle distillates is one of the key processes in modern refining technology. Results of hydrotreating of gas oil and LCO blends, obtained in an industrial hydrotreater, are presented. Increasing temperature differences in the reactor with increasing content of LCO in the blend were observed along with substantial decrease of total sulfur in the product. A mathematical model of the industrial hydrotreater was developed to simulate the reactor behavior under different operating conditions. Cubic EOS were applied to model VLE of the reacting fluid for the ternary mixture composed of hydrogen, methane, and n-hexadecane. Validation of the model was performed using the available data obtained during the industrial test run. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering-7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).
Source:
19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congres, 2010
Publisher:
19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7
TY - CONF
AU - Dukanović, Z.
AU - Duričković, I.
AU - Glišić, Sandra
AU - Orlović, Aleksandar
PY - 2010
UR - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/1552
AB - Hydrotreating of middle distillates is one of the key processes in modern refining technology. Results of hydrotreating of gas oil and LCO blends, obtained in an industrial hydrotreater, are presented. Increasing temperature differences in the reactor with increasing content of LCO in the blend were observed along with substantial decrease of total sulfur in the product. A mathematical model of the industrial hydrotreater was developed to simulate the reactor behavior under different operating conditions. Cubic EOS were applied to model VLE of the reacting fluid for the ternary mixture composed of hydrogen, methane, and n-hexadecane. Validation of the model was performed using the available data obtained during the industrial test run. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering-7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).
PB - 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7
C3 - 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congres
T1 - Modelling of industrial trickle-bed reactor for hydrotreating of gas oil and light cycle oil blends
UR - https://hdl.handle.net/21.15107/rcub_technorep_1552
ER -
@conference{
author = "Dukanović, Z. and Duričković, I. and Glišić, Sandra and Orlović, Aleksandar",
year = "2010",
abstract = "Hydrotreating of middle distillates is one of the key processes in modern refining technology. Results of hydrotreating of gas oil and LCO blends, obtained in an industrial hydrotreater, are presented. Increasing temperature differences in the reactor with increasing content of LCO in the blend were observed along with substantial decrease of total sulfur in the product. A mathematical model of the industrial hydrotreater was developed to simulate the reactor behavior under different operating conditions. Cubic EOS were applied to model VLE of the reacting fluid for the ternary mixture composed of hydrogen, methane, and n-hexadecane. Validation of the model was performed using the available data obtained during the industrial test run. This is an abstract of a paper presented at the 7th European Congress of Chemical Engineering-7 and the 19th International Congress of Chemical and Process Engineering CHISA (Prague, Czech Republic 8/28/2010-9/1/2010).",
publisher = "19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7",
journal = "19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congres",
title = "Modelling of industrial trickle-bed reactor for hydrotreating of gas oil and light cycle oil blends",
url = "https://hdl.handle.net/21.15107/rcub_technorep_1552"
}
Dukanović, Z., Duričković, I., Glišić, S.,& Orlović, A.. (2010). Modelling of industrial trickle-bed reactor for hydrotreating of gas oil and light cycle oil blends. in 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congres
19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7..
https://hdl.handle.net/21.15107/rcub_technorep_1552
Dukanović Z, Duričković I, Glišić S, Orlović A. Modelling of industrial trickle-bed reactor for hydrotreating of gas oil and light cycle oil blends. in 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congres. 2010;.
https://hdl.handle.net/21.15107/rcub_technorep_1552 .
Dukanović, Z., Duričković, I., Glišić, Sandra, Orlović, Aleksandar, "Modelling of industrial trickle-bed reactor for hydrotreating of gas oil and light cycle oil blends" in 19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congres (2010),
https://hdl.handle.net/21.15107/rcub_technorep_1552 .
