The Effects of Supercritical Propane on the Alkylation of Toluene with Ethylene over USY and Sulfated Zirconia Catalysts

Daniel M. Ginosar,* Kyle Coates, and David N. Thompson
Idaho National Engineering and Environmental Laboratory, P.O. Box 1625, Idaho Falls, Idaho 83415-2208
Ind. Eng. Chem. Res., 2002, 41 (25), pp 6537–6545
DOI: 10.1021/ie0202569
Publication Date (Web): November 13, 2002
Copyright © 2002 American Chemical Society
*

 Corresponding author:  Daniel M. Ginosar. Phone:  (208) 526-9049. E-mail:  dmg@inel.gov. Fax:  (208) 526-8541.

 Phone:  (208) 526-6994. E-mail:  kam2@inel.gov.

 Phone:  (208) 526-3977. E-mail:  thomdn@inel.gov.

Abstract

The alkylation of toluene with ethylene over microporous USY zeolite and mesoporous sulfated zirconia (S/ZrO2) catalysts was explored at liquid, near-critical liquid, and supercritical conditions using propane as the supercritical cosolvent. Liquid, near-critical liquid, and supercritical conditions were examined for their effects on product selectivity and catalyst activity maintenance. The S/ZrO2 catalyst demonstrated alkylation activity almost exclusively, whereas the USY catalyst demonstrated both alkylation and cracking/disproportionation activities. Near-critical and supercritical reaction conditions improved product selectivity with the USY catalyst through the suppression of disproportionation reactions and enhanced ortho- and para-ethyltoluene selectivity. However, the addition of the supercritical cosolvent resulted in increased deactivation for both the S/ZrO2 and USY catalysts, with deactivation increasing with propane mole fraction.

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History

  • Published In Issue December 11, 2002
  • Received for review April 5, 2002
    Revised manuscript received September 26, 2002
    Accepted September 26, 2002

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