The direct alkylation of toluene with ethane to the isomeric ethyltoluenes and hydrogen using a bifunctionalPd/H-ZSM-5 catalyst was carried out in a fixed-bed, flow-type reactor. The effect of pressure was investigatedbetween 1 and 100 bar and at moderate temperatures of 300 and 350
C. From stoichiometry, no influenceof pressure is expected for ideal gases. However, thermodynamic equilibrium calculations for a network ofreactions, taking into account
nonideal gas behavior, do predict an influence of pressure. Toluene conversionsof 5-8% observed experimentally at 300
C over the entire pressure range are in line with these calculations.In contrast, the toluene conversion observed at 350
C and 50 bar is at 27% well above the equilibrium valuecalculated using a limited reaction network. It is proposed that the formation of hydrogen-rich light alkanesis favored at high pressures, creating a
hydrogen sink. Hence, the equilibrium is shifted toward the formation of ethyltoluenes. The maximum experimental yield of ethyltoluenes achieved so far is approximat
ely14 wt %.