Evaluacion de catalizadores de W-Ni-Pd Y W-Ni soportados sobre Al 2 O 3 -TiO 2 empleando como reaccion modelo la hidrogenacion de benceno en presencia de dimetildisulfuro

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

Zuleima Karpyn, S. Marzuka, J. Trujillo, J. Papa

Research output: Contribution to journalArticle

Abstract

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.

Original languageSpanish
Pages (from-to)55-60
Number of pages6
JournalRevista de la Facultad de Ingenieria
Volume16
Issue number1
StatePublished - Oct 10 2001

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Catalyst supports
Hydrogenation
benzene
Benzene
catalyst
Catalysts
pressure effect
Pressure effects
Packed beds
temperature effect
Thermal effects
temperature
Temperature
liquid
Liquids
evaluation
reactor

All Science Journal Classification (ASJC) codes

  • Engineering(all)
  • Earth and Planetary Sciences(all)

Cite this

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abstract = "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.",
author = "Zuleima Karpyn and S. Marzuka and J. Trujillo and J. Papa",
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AU - Karpyn, Zuleima

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AU - Trujillo, J.

AU - Papa, J.

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N2 - 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.

AB - 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.

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