Cumene hydroperoxide (CHP) has been used as an initiator in polymerization
and catalytic cleavage in the production process of phenol and acetone. It
is usually produced by the cumene oxidation reaction. In its manufacturing
processes, many explosion and fire incidents are caused by this material ow
ing to its thermal instability or incompatibility in its oxidation reaction
or concentrated processes. Thus, the reactive hazard on this material has
to be clearly identified and its critical runaway temperature and unstable
reaction criterion has to be determined. In this investigation, the critica
l runaway temperature and stable reaction criterion with the initial concen
trations of 15 wt% and 20 wt% CHP in its reaction processes were evaluated
from their reaction kinetic parameters. The results are important and usefu
l in the production, transportation and storage processes of CHP. (C) 2001
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