This study aims to
convert ethanol to higher value-added products,
particularly diethyl ether and ethylene using the catalytic dehydration
of ethanol. Hence, the gas-phase dehydration of ethanol over Al2O3-HAP catalysts as such and modified by addition
of palladium (Pd) in a microreactor was evaluated. The commercial
Al2O3–HAP catalyst was first prepared
by the physical mixing method, and then, the optimal ratio of the
Al2O3–HAP catalyst (2:8 by wt %) was
impregnated with Pd to develop a new functional catalyst to alter
surface acidity. Based on the results, the combination of Al2O3 and HAP catalysts generated significant quantities
of weak acid sites which demonstrates an enhancement in catalytic
activity. In addition, Pd modification in the optimal composition
ratio of the Al2O3–HAP catalyst extremely
increased the amount of weak acid sites as well as weak acid density
due to the synergistic effect between the Pd and Al2O3–HAP catalyst that are supposed to suggest the active
sites in the reaction. Among all catalysts, the Al20-HAP80-Pd catalyst
displayed brilliant catalytic performance in the course of diethyl
ether yield (ca. 51.0%) at a reaction temperature of 350 °C and
ethylene yield (ca. 75.0%) at a reaction temperature of 400 °C
having an outstanding stability under time-on-stream for 10 h. This
is recognized to the combination of the effects of weak acid sites
(Lewis acidity), small amount of strong acid sites, and structural
characteristics of the catalytic materials used.