The catalytic activity and selectivity of a series of AlPO 4 and AlPO 4-metal oxide systems (Al 2O 3, TiO 2, and ZrO 2 with an AlPO 4/metal oxide weight ratio of 3) were investigated at temperatures ranging from 673 to 873 K for the gas-phase microcatalytic alkylation of toluene with methanol. The results show that AlPO 4's catalyst exhibits surface acid sites accessible to toluene molecules that are strong enough to alkylate in the presence of methanol. The methylation of toluene produces a mixture of xylenes (XY) as principal products, although 1,2,4-and 1,2,3-trimethylbenzenes (TMB) were also found to be dialkylation products for AlPO 4-Al 2O 3 catalysts. The formation of TMB is associated with a parallel decline in o-XY and p-XY selectivity. Furthermore, in all cases, scarcely any side-chain-methylation of toluene to ethylbenzene (ETB) is found. The alkylation reaction follows the Bassett-Habgood kinetic equation for first-order reaction processes in which the surface reaction is the controlling step. The influence of the reaction temperature, pulse number, and toluene/methanol molarity upon the conversion of toluene and the selectivities of the products were investigated. The activity of AlPO 4 and AlPO 4-metal oxide catalysts in the ring-methylation of toluene decreases in the order AlPO 4Al 2O 3 > AlPO 4 > AlPO 4TiO 2 > AlPO 4ZrO 2. This order is relatively well interpreted in basis to the surface acid properties studied gas-chromatographically through the irreversible adsorption of pyridine at temperatures in the range 473 to 673 K. This indicates that Brønsted acidity decreases when Al 2O 3 is substituted by TiO 2 or ZrO 2 in the AlPO 4-metal oxide system. OPE (Optimum Performance Envelope) curves on product selectivity plots show that ETB and XY are competitive primary reaction products, while TMB are stable secondary reaction products. In all cases, the selectivity decreases in the order S XY > S TMB > S ETB.
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