The catalytic conversion of methanol to dimethyl ether (DME) has been
studied over a series of solid-acid catalysts, such as gamma-Al2O3, H-
ZSM-5, amorphous silica-alumina, as well as titania modified zirconia.
All the catalysts are active and selective for DME formation. The app
arent activation energy for DME formation over gamma-Al2O3 is ca. 25 k
cal/mol, a value that increases to ca. 37 kcal/mol upon the addition o
f 23 Torr of H2O to the reagent. The rate of methanol dehydration decr
eases with increasing acidity (silica content) over the amorphous sili
ca-alumina catalysts. Although H-ZSM-5 with Si/AL = 25 is the most act
ive among the catalysts tested, the DME selectivity is only 20% at 280
degrees C, a typical temperature used in the syngas-to-methanol proce
ss. An amorphous silica-alumina catalyst with 20 wt.-% silica content
(SIRAL20) exhibits the best catalytic performance of those tested at 2
80 degrees C.