Pressure and temperature effects on the liquid-phase hydrogenation of benzene over W-Ni-Pd/(Al 2 O 3 -TiO 2 ) and W-Ni/(Al 2 O 3 -TiO 2 ) catalysts were evaluated. Experimental runs were conducted using a tubular packed bed reactor Operated within a pressure range of 400 to 700 psi, and a temperature range of 320 to 350°C. Experimental results showed that the conversion increases with an increase in pressure and in temperature. Besides, an activity increase is observed with Pd promoted catalyst.
|Translated title of the contribution||Evaluation of W-Ni-Pd and W-Ni catalyst supported over Al 2 O 3 -TiO 2 using the reaction model of hydrogenation of benzene in the presence of dimethyldisulfide|
|Number of pages||6|
|Journal||Revista de la Facultad de Ingenieria|
|State||Published - Oct 10 2001|
All Science Journal Classification (ASJC) codes
- Earth and Planetary Sciences(all)