M.I. Zaki et al. / Thermochimica Acta 311 (1998) 97±103
101
and 8008C. The former four bands are assignable to a
mixture of Mn2O3 and Mn3O4 [14], whereas the latter
two bands are most likely due to highly distorted MnO
[15]. These results may imply that the TG-displayed
single WL step for the CO-reduction of test samples is
somewhat composite in nature and conceals a multi-
step course to the eventual reduction product (MnO).
The fact that the CO-reduction of the test MnOx
materials to MnO is completely suppressed, or com-
pensated for, in the mixed atmosphere of COO2 may
imply either complete unavailability of CO, or simul-
taneous re-oxidation by the coexisting O2. The beha-
viour communicated for MnO2 and Mn5O8, in
particular, may rather sustain the CO unavailability
option. The corresponding TG curves (Fig. 3) do not
display the tendency of both the test materials towards
the required dissociative uptake of O2. Consequently,
the CO molecules have most likely been catalytically
oxidized in the oxygen-rich atmosphere over the
operational temperature range of the CO-reduction
of the test oxides, i.e. at 200±5008C (Fig. 2). The
subsequent WG observed detectably at 500±10008C
for Mn5O8 (Fig. 3(B)) and Mn2O3 (Fig. 3(C)), may be
ascribed tentatively to CO2 absorption by the test
materials.
3.3. TG curves in COO2 atmosphere
TG curves obtained on heating the test Mn-oxides
in a mixed atmosphere of COO2 (1 : 2) are displayed
in Fig. 3, which also insets, for comparison purposes,
the TG curves obtained for the given oxide in the
separate gas atmospheres of CO (Fig. 2) and O2
(Fig. 1). The results help to characterize either of
the following two behaviours: (i) a behaviour to which
both CO and O2 have comparably contributed, and (ii)
a behaviour to which O2 is the dominant contributor.
The former behaviour is the one re¯ected by the TG
curves of MnO2 (Fig. 3(A)), Mn5O8 (Fig. 3(B)) and
Mn2O3 (Fig. 3(C)), whereas the latter is the one
monitored by the TG curves of Mn3O4 (Fig. 3(D))
and MnO (Fig. 3(E)).
GC analysis results of the COO2 stream at RT, and
following heating over MnO2 to 300 and 7008C are
shown in Fig. 4. These results show the formation of
CO2 at 300 and 7008C. IR analysis of the solid
residues of MnO2 characterizes Mn5O8 (bands at
1
424(w,sh), 493(s,sp) and 608(s,sp) cm
[7]) and
For MnO2, Fig. 3(A) reveals that the coexistence of
CO in the surrounding gas atmosphere accelerates the
thermal decomposition to Mn5O8 (possibly plus
Mn2O3) to commence near 5008C instead of 6308C
in pure O2. On the other hand, the coexistence of O2
may be seen to completely suppress, or compensate
for, the reductive in¯uence of CO; the reductive WL
step commencing near 3508C in the CO atmosphere is
not visible in the mixed atmosphere of COO2
(Fig. 3(A)). A similar behaviour can be seen in
Fig. 3(B) and (C) for Mn5O8 and Mn2O3, respectively.
The results reveal, for both materials, a complete
suppression of the CO-reduction, due to the coexis-
tence of O2, and show alternatively a steady WG till
the decomposition temperature (near 10008C) of
Mn2O3 to Mn3O4 is reached.
For Mn3O4, the TG obtained in COO2 (Fig. 3(D))
is largely similar to that obtained in pure O2. Thus, the
CO-reduction to MnO is completely prevented,
whereas the oxidation to Mn2O3 is maintained. The
same is shown (Fig. 3(E)) to apply to MnO. The sole
difference here lies in the fact that CO originally has
no reductive in¯uence on MnO over the temperature
range scanned.
Mn2O3 (bands at 429(w,sh), 494(s,sp), 604(s,sh) and
694(w,sh) cm 1 [14]) following heating in COO2 to
400 and 6008C, respectively. Consequently, it is not
until the temperature reaches 4008C that MnO2 com-
mences to reduce in COO2, and the reduction pro-
duct, even at 6008C, is not MnO. Thus, the catalytic
COO2 reaction (at 3008C in particular) is the
only source left for CO2 production in the gas
phase [16].
The above results indicate that all of the MnOx
compositions tested, except for MnO, exhibit catalytic
activity towards CO oxidation in O2-rich atmosphere.
However, the higher thermal stabilities of composi-
tions in the range MnO1.5±1.3, i.e. in the Mn2O3Ð
Mn3O4 system, might render them particularly inter-
esting in the ®eld of applied catalysis. The failure in
detecting carbon deposits on the solid residues of the
heating of MnO2 in COO2 atmosphere at 6008C may
exclude the Boudouart mechanism (2CO(g)!CO2(g)
C(s) [17]) from the likely surface reaction pathways of
CO oxidation [16]. It may, alternatively, suggest Mn-
oxides as promising ingredients for the catalyst being
sought [4] for soot combustion in automobile exhaust
emissions.