Catalytic hydrotreating of heavy gasoil FCC feed over a NiMo/γ-Al2O3-TiO2 catalyst: Effect of hydrogen sulfide on the activity

Javier Herbert, Víctor Santes, Maria Teresa Cortez, René Zárate, Leonardo Díaz

Producción científica: Contribución a una revistaArtículorevisión exhaustiva

11 Citas (Scopus)

Resumen

An experimental study was conducted in a pilot plant fixed-bed reactor in order to evaluate the effect of hydrogen sulfide on hydrotreating activity of an industrial heavy gasoil Fluid Catalytic Cracking (FCC) feed recovered from a Mexican refinery. Hydrotreating reactions were carried out at three temperatures (603, 638 and 673 K), 11.76 MPa of pressure and LHSV of 6 h-1. Studies were done varying hydrogen sulfide concentration 0, 100, 450 and 750 vol ppm (0, 3100, 12,960 and 23,210 Pa, respectively) at the same operating conditions over a commercial NiMo/γ-Al2O3-TiO 2 catalyst. Experimental results showed different behavior for these reactions. An inhibiting effect on hydrodesulfurization (HDS), hydrodearomatization (HDA) and hydrodenitrogenation (HDN) was observed, whereas the hydrodemetallization (HDM) reaction showed an increase in the activity. Apparent activation energies were also determined for each reaction.

Idioma originalInglés
Páginas (desde-hasta)559-563
Número de páginas5
PublicaciónCatalysis Today
Volumen107-108
DOI
EstadoPublicada - 30 oct. 2005

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