The decomposition of cumene hydroperoxide (CHP) was carried out in a batch
reactor over supported solid acid catalysts, acid-activated montmorillonite
K10 (Mont. K10) and metal-ion-exchanged (Mont. K10), at 30-60 degreesC. Th
e products were phenol and acetone. Supported dodecatungstophosphoric acid
(DTPA) showed 100% conversion within 5 min at 30 degreesC; the results obta
ined over acid-activated (Mont. K10) were also comparable. The type of acid
ity and the strength were determined. The correlation of catalytic activity
with acidity revealed that both Lewis and Bronsted acid sites promote the
decomposition. The reaction was first-order with respect to CHP. The result
s indicate that heterogeneous catalysts may be used instead of sulfuric aci
d for selective decomposition of CHP into phenol and acetone with 100% conv
ersion. (C) 2001 Elsevier Science B.V. All rights reserved.