The CO2 evolution curve from MSWI fly ash (FA) and model systems containing
different carbon species was studied by means of the TG-FTIR technique. Th
e number of peaks in the curves depends on the system studied. one peak is
observed from activated carbon, C-act in model mixtures with silica, SiO2,
or whereas two from C-act-CUCl2-SiO2. This, together with the higher C-act
reactivity in the two-peak system indicates the catalytic effect of Cu ion.
Moreover, this effect is dependent on the copper compound: adding copper a
s CuO or CuSO4 does not change the CO2 evolution curve in comparison with t
he uncatalyzed C-act-SiO2 system. Two peaks were also observed for the C-na
t-TTFA (Thermally Treated Fly Ash) and C-nat-TTFA systems (C-nat is the "na
tive" carbon, i.e., the unburnt unextractable organic carbon from FA). The
behavior of amorphous carbon systems, C-amoiphous-SiO2 and C-amorphous-TTFA
, was different as two peaks were observed in both cases; this was explaine
d by comparing the Raman spectra of amorphous carbon with respect to those
of the native and activated carbon. Finally,two peaks were observed in the
CO2 evolution curves from raw FA and fractions obtained from it. Thus, it i
s possible to conclude that low temperature native carbon gasification is h
ighly dependent on the catalyst added to the model mixtures as well as on t
he metal already present in the TTFA or raw FA. This conclusion supports pr
evious findings from kinetic studies. The results obtained are also importa
nt to explain the formation reactions of organochlorinated micropollutants.
The influence of initial organic carbon content is also discussed.