Pdydhyy adverse impacts of oil pollution with serious and destructive on the environment and human health. Since one of the main sulfur compounds Lvdhknndhhay oil refinery and one of the most important are the objectives in this study a systematic review in order to determine the reaction kinetics of hydrogen desulfurization) HDS diesel oil cut using a commercial catalyst was NHS $ -204 $. Reactive tests in a tiny bed temperature Qtrhyy $ 360-380 ^ degree C $, pressure and velocity space bar 70-55) LHSV (h $ ^ {-1} $ 2-0.5 done. According to the desulfurization especially derivatives of Tyvfnha Dybnzvtyvfny Bnzvtyvfny and is difficult and comes in deep desulfurization, so here the reaction kinetics (HDS) for the article Dybnzvtyvfn and sulfur can form model was determined. The results indicate that the degree of reaction in the feed gasoline HDS Dybnzvtyvfn is equal to 1.4. HDS reaction activation energy was determined as the kcal/mol15.
Ganji, H. (2009). Deep desulfurization reaction kinetics for hydrogen-gasoline cutting oil. Sharif Journal of Mechanical Engineering, 25(No . 50), 47-53.
MLA
Hamid Ganji. "Deep desulfurization reaction kinetics for hydrogen-gasoline cutting oil". Sharif Journal of Mechanical Engineering, 25, No . 50, 2009, 47-53.
HARVARD
Ganji, H. (2009). 'Deep desulfurization reaction kinetics for hydrogen-gasoline cutting oil', Sharif Journal of Mechanical Engineering, 25(No . 50), pp. 47-53.
VANCOUVER
Ganji, H. Deep desulfurization reaction kinetics for hydrogen-gasoline cutting oil. Sharif Journal of Mechanical Engineering, 2009; 25(No . 50): 47-53.
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