作者: A. Gutiérrez , J. M. Arandes , P. Castaño , M. Olazar , A. Barona
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摘要: The effect of temperature has been studied in hydrocracking light cycle oil (LCO), byproduct fluidized catalytic cracking (FCC) units on a bifunctional catalyst (Pt-Pd/HY zeolite). increase both and H2 partial pressure have an important attenuating deactivation, given that they decrease sulfur equilibrium adsorption enhance coke precursors. Therefore, the maintains significant hydrodesulfurization activity. As is increased, conversion naphtha selectivity increase, although there no dearomatization medium distillate fraction range experimental conditions. 400 °C more suitable for obtaining high yield with content i-paraffins.