Photocatalyzed oxidation of ethanol and acetaldehyde in humidified air
was carried out to establish a first complete kinetic model for a pho
tocatalyzed multispecies network. Two photocatalysts were examined in
a batch, recirculation reactor, near-UV illuminated TiO2 (anatase) coa
ted (i) on the surface of a nonporous quartz glass plate and (ii) on a
porous ceramic honeycomb monolith. The former contained only illumina
ted (active) surfaces, the latter consisted of substantial ''dark'' su
rfaces coated with a thin layer of illuminated (active) catalyst. Etha
nol was photooxidized to acetaldehyde and formaldehyde intermediates,
and eventually to carbon dioxide and water products. The catalyst and
monolith surfaces adsorbed appreciable fractions of the trace ethanol,
acetaldehyde, formaldehyde, carbon dioxide, and water present. Ethano
l, acetaldehyde, and carbon dioxide adsorption isotherms were measured
on both catalysts; the formaldehyde adsorption isotherms were assumed
identical to those of acetaldehyde. On the fully illuminated glass pl
ate reactor, all four species were accounted for, and closure of a tra
nsient carbon mass balance was demonstrated. Completion of a transient
carbon balance on the monolith reactor required inclusion of addition
al reaction intermediates (acetic and formic acids), which appear to r
eversibly accumulate on only the dark surfaces. The ethanol and acetal
dehyde photocatalyzed oxidation kinetic networks were modeled using La
ngmuir-Hinshelwood rate forms combined with adsorption isotherms for r
eactant, intermediates, and product CO2 For both the quartz plate and
monolith catalysts, satisfactory kinetic models were developed to pred
ict the entire time course of ethanol and acetaldehyde multicomponent
batch conversions. (C) 1996 Academic Press, Inc.