2007
DOI: 10.1016/j.fuel.2006.09.019
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Trickle bed reactor model to simulate the performance of commercial diesel hydrotreating unit

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Cited by 36 publications
(27 citation statements)
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“…where, L r : bed length of the reactor (cm); D r : reactor diameter (cm); 3 1 : liquid phase fraction; D r L : radial mass dispersion coefficient (cm 2 s À1 ); u l : supercial liquid velocity (cm s À1 ) The percentage of the liquid phase can be determined from the following empirical relation: 56 .…”
Section: Optimal Ratio Of (L R /D R )mentioning
confidence: 99%
“…where, L r : bed length of the reactor (cm); D r : reactor diameter (cm); 3 1 : liquid phase fraction; D r L : radial mass dispersion coefficient (cm 2 s À1 ); u l : supercial liquid velocity (cm s À1 ) The percentage of the liquid phase can be determined from the following empirical relation: 56 .…”
Section: Optimal Ratio Of (L R /D R )mentioning
confidence: 99%
“…Hydrotreating is a process in which the feed stream, practically any fraction of the oil, reacts with hydrogen at high pressures and temperatures in the presence of a heterogeneous catalyst (Korsten and Hoffmann, 1996;Murali et al, 2007). According to Aye and Zhang (2005) and Ferreira et al (2013), kinetic models are fundamental for a good performance of the HDT simulation, and the optimization of the hydrotreatment process can benefit from reliable kinetic models of the hydrodesulfurization reactions, among others.…”
Section: Introductionmentioning
confidence: 99%
“…O HDT de diesel é feito com o uso de um reator de leito gotejante (Trickle Bed Reactor -TBR) que permite a redução do teor de enxofre e de outros contaminantes. Desta forma, as correntes de óleo diesel a ser hidrotratado e de hidrogênio fluem através de um leito fixo de catalisador (Murali et al, 2007).…”
Section: Introductionunclassified