Abstract

We present an analysis of mass transfer in solid-liquid phase-transfer catalysis (SLPTC), obtaining analytical solutions for the stagnant-film model and numerical solutions to the complete transport equations for the von Kármán rotating-disk flow. The latter is viewed as a prime candidate for experimental studies on SLPTC. A catalyst-effectiveness plot is developed, which displays both mass-transfer enhancement and reaction-rate limitation associated with the two distinct Damköhler parameters for the bulk and surface reactions. Solutions are obtained from the film model for pseudo-first-order reaction and for rapid equilibrium reaction, including irreversible reaction with flame-like reaction fronts. Comparison of stagnant-film model against the numerical solutions for the rotating disk shows generally good agreement, as one would expect for uniformly accessible surfaces.

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call