Thermal incineration of carbon monoxide (CO! has been evaluated using
published kinetic data. Profiles of residence time versus fractional C
O oxidation have been calculated and used in order to estimate inciner
ator size and auxiliary fuel requirements. The calculation procedure i
ncludes the effect of the reaction exotherm, under both adiabatic and
non-adiabatic conditions. An apparent mean temperature of incineration
may therefore be determined. This apparent mean will differ from the
arithmetic mean of the stream temperatures to and from the incinerator
and appreciable error may result if the arithmetic mean is used to ca
lculate incineration time. The calculations have confirmed that CO is
more difficult to oxidize than many volatile organic compounds (VOCs)
and the rate of oxidation of intermediate CO should be included in eva
luation of VOC incineration. Short residence times, of 0.5 seconds or
less, favour minimization of both incinerator size and auxiliary fuel
requirements for thermal incineration of both CO and VOCs. The optimum
range of residence time for 99.5% CO incineration at an initial tempe
rature of 1045 It appears to be approximately 0.3 to 0.4 seconds.