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limited by the light absorption in a zero-order reaction
process. As shown in Fig. 6c, for un-coated TiO2 after
200 min the reaction proceeds well in accordance with a
logarithmic relationship, but its first-order reaction rate
constant is 36 9 10-5 min-1 is smaller than that of
176 9 10-5 min-1 for silica-coated TiO2. This is because,
without silica, the catalyst surface will be altered in the first
200 min. In contrast to this, for the catalyst modified with
silica, the reaction appeared to be first-order, and it
remained relatively stable from the start of the irradiation,
so that the coated-silica increased the transfer rate of
acetaldehyde to the TiO2 reactive sites and the reaction site
was not suppressed by the intermediates.
(a)
(b)
Now let us move on the toluene decomposition in Fig. 4
to discuss the effect of silica modification. Figure 7b shows
that, in the first stage of the reaction, the reaction proceeds
determined by light absorption with a zero-order reaction
rate constant of 11.4 ppm/min for silica-coated TiO2,
which is slightly smaller than that of 14.4 ppm/min for
un-coated TiO2. Both the decomposition rates quickly
decreased during the irradiation, but the decrease for
un-coated TiO2 fell faster than the silica-coated counter-
part. After 3 min from the start of the irradiation, silica-
coated TiO2 overtook the un-coated one in the formation of
CO2. The period of the reaction limited by the light
absorption was very short, indicating that the TiO2 surface
adsorbed many kinds of intermediates caused by side
reactions and gradually decreased the reaction rate. Con-
trary to the case of acetaldehyde decomposition, in which
the reaction rate was not decreased with silica-coating, the
rate of toluene decomposition fell off. This is probably
because the intermediates generated by toluene decompo-
sition imposed the load to reach the final product of CO2.
Figure 7c shows that the first-order reaction rate constant
k1 for un-coated TiO2 was 6.5 9 10-5 min-1; while that
Fig. 8 Plausible reaction scheme showing the effect of SiO2 coating
on the decomposition of organic substances. a un-coated titanium
dioxide. b silica-coated titanium dioxide
reaction rate constant, with r0 = 7r for the toluene
decomposition reaction expressed by Eq (6). Hence, the
first-order reaction rate constant, k1, can be obtained from
the logarithm of the relative increase in CO2 concentration.
As shown in Figs. 6c and 7c, after irradiation for a few
hours this equation held for both reactions with the two
differential photocatalysts.
Generally speaking in photocatalytic reactions,
a
decomposition reaction whose rate is limited by the light
absorption (Eq 7) will change to that whose rate is limited
by mass transfer (Eq 90), because the amount of the reac-
tant decreases during the reaction and the concentration
becomes low relative to the amount of the active sites
resulting in a first-order reaction. When the reactant gen-
erates several kinds of stable intermediates, the reaction
process that leads to the final product CO2 may be pro-
longed, resulting in the deviation of the time dependencies
of zero- or first-order reaction kinetics stated above.
for silica-coated TiO2 was as large as 14.5 9 10-5 min-1
.
Hence, the mass transfer of toluene to reactive sites must
be faster for silica-modified TiO2. According to a very
recent report [18], the decomposition rate is reduced due to
silica promoting separation of the generated intermediates
from the catalyst surface. Therefore it is probable that
decomposition intermediates cover the oxidation sites
(surface-trapped holes) as schematically shown in Fig. 8.
Hence, the high photocatalytic activity observed for the
silica modified TiO2 may be due to that the intermediates
were adsorbed on silica and does not block the oxidation
sites of TiO2. It has been reported already that, when the
silica coating layer was incomplete, the photocatalytic
activity of coated nanoparticles was higher than that of
TiO2 nanoparticles, while, when the surface of TiO2 was
coated completely, the activity sharply decreased [9].
As stated earlier, coating TiO2 with silica is a well-
known technique for practical applications. It is also widely
Taking these factors into account, let us discuss the
effect of silica coating on the photocatalytic reactions.
Photocatalytic decomposition of acetaldehyde was shown
in Fig. 6 as the time profile of CO2 evolution. Un-coated
TiO2 in Fig. 6b shows a zero-order reaction rate constant as
large as 14.2 ppm/min at the initial stage, but, after the first
few minutes, the rate is suddenly decreased, indicating the
suppression of the reaction sites by the reaction interme-
diates. In contrast, for silica-coated TiO2 in Fig. 6b,
although its initial reaction rate is as small as 2.0 ppm/min,
there is a linear increase in CO2 concentration for more
than 10 min, which indicates that the reaction rate was
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