Abstract
Titanium silicalite-1 (TS-1) tubular membrane was used as a catalytic active membrane reactor in the oxidation of iso-propanol with hydrogen peroxide. The TS-1 membrane prepared at 150°C showed the highest catalytic activity with the conversions above 90%. The kinetic parameters of the reaction were calculated and a simple column mathematical model was used to describe the catalytic activity of the membrane reactor.
