44
A.M. Banerjee et al. / Thermochimica Acta 516 (2011) 40–45
Table 2
after reduction generates the active metal that can dissociate and
activate the hydrogen for facilitating an otherwise difficult reduc-
tion phenomenon. It is reported [22,23] that hydrogen spillover
can be broken into three primary steps: (i) dissociative chemisorp-
tion of gaseous H2 on a transition metal catalyst; (ii) migration of
H atoms from the catalyst to the substrate and (iii) diffusion of H
atoms on substrate surfaces and/or in the bulk materials. In this
case the metallic Ni formed after reduction is the transition metal
catalyst. The substrate is the remnant oxide from which Ni2+ cation
gets eliminated and then the reduction of bulk In3+ occurs by dif-
fusion of H-atoms into the remnant oxide material and thus the
reduction profile shifts to lower temperature. Diffusion of H atoms
and subsequent reduction of Ti4+ is definitely easier in NiTiO3 that
the indium titanate phase so we observe higher amount of Ti4+
reduction in the sample. This is further corroborated by the TPR
results where we observe increased hydrogen consumption dis-
crepancy with an increase in Ni content. Alloy formation of the
transition metal catalyst Ni with In and Ti prevented further reduc-
carbon, where hydrogen spillover is mainly responsible in increas-
ing the storage capacity [24]. Recently, pioneering studies by Yang
et al. revealed novel processes to store substantial quantities of
hydrogen via hydrogen spillover [25–27].
Representative XPS binding energy values of different elements in ITN4 samples
obtained before and after the first TPR cycle in temperature range of 25-1100 ◦C.
BE of XPS signal (eV)
Before TPR
After TPR
Elements
B.E
Oxidation state
In 3d5/2
445.9
+3
Ti 2P3/2
457.5
+4
In 3d5/2
444.1
0
Ti 2P3/2
457.5, 453.7
+4, 0
In3+
No peak due to
In0
Ti4+, Ti0
Ti0 metal
In the reduced sample, in addition to major peak at 457.5 eV a
shoulder is observed at 453.7 eV corresponding to Ti(0) state. The
appearance of this shoulder peak confirms the reduction of Ti4+
to Ti metal during the temperature programmed reduction (TPR)
experiments. In addition, in Fig. 5a, a shoulder appears at higher
binding energy in the XPS spectra of Indium ion for the fresh sam-
ple, but it completely disappears in the spectra recorded after the
complete reduction. The appearance of shoulder is attributed to the
interaction of In3+ with other ions present in the compound. Thus as
process of reduction proceeds, the interaction of Indium with other
ions decreases or it gets segregated out from the sample. However,
presence of In 1+ in the reduced sample is not observed as observed
earlier for partially reduced sample in case of iron substitution [20].
Intensity of In (3d) peak is considerably increased in Fig 5a, after
complete reduction as compared to fresh sample. Thus, ITN4, sam-
ple on reduction, deposits the metallic Indium on the surface and
hence the peak intensity due to Indium on surface increases. It is
well known that the catalytic properties of a sample are sensitive
to its surface composition; therefore this observation may play a
crucial role in deciding its performance for redox reactions. The
XPS results in accordance with TPR and thermogravimetry results
suggests the formation of metallic Ti(0) along with Ti4+ and In (0)
when ITN4 was reduced in H2 up to 1100 ◦C whereas unsubstituted
In2TiO5 did not reveal any reduction of Ti4+ species. Thus presence
of Ni influenced the reduction behavior of Ti4+ species present in
the sample by activating H2 molecules.
5. Conclusions
A-site substitution by a divalent Ni2+ cation at In3+ site of
In2TiO5 resulted in single phase compositions at low extent of
substitution (up to 5%), biphasic at a higher substitution (10%)
with very low impurity phase of unreacted NiO and triphasic
at even higher Ni content (15–20%), having very low concentra-
tions of NiO and NiTiO3 phase. The temperature programmed
reduction, XRD and XPS studies establishes complete reduction
of In3+ and Ni2+ to In0 and Ni0 states in temperature range of
450–1100 ◦C in all the samples. Ni substitution induced consider-
able ease in reducibility (Tmax) of substituted samples as compared
to In2TiO5 phase. The substitution-induced non-stoichiometry and
the microstrucural defects may cause the distortion in the lattice,
thus facilitating the reduction of oxides. The interesting obser-
4. Discussion
The reduction of In2(1−x)Ni2xTiO5−ı oxide samples is represented
by following equation:
vation was the reduction of otherwise non-reducible cation Ti4+
,
◦
in the 20% substituted sample, ITN4. Ni metal initially formed
by the reduction of Ni2+ dissociate and activate the hydrogen
which eased the In3+ reduction and even facilitated the reduc-
tion of Ti4+. Metallic Ni and In reacts to form ıIn3Ni2 alloy
while metallic Ni and Ti reacts to form an alloy Ti2Ni. Due to
the formation of these alloys the rate of hydrogen adsorption
diminishes, which slows down further hydrogen activation and
In2(1−x)3+Ni2x2+Ti4+O5−ı(s) + (3 − ı)H2(g)490−−1→100 2(1 − x)In0(s)
+ 2xNi0(s) + Ti4+O2(s) + (3 − ı)H2O(g)
C
H2 consumption data calculated as well as that observed from
the areas under TPR peak, for all samples for the first reduction
for ITN1 for all other samples experimental values are higher than
calculated values. This discrepancy increases with increase in Ni
content as observed from Table 3. It can be explained on the basis
of autocatalytic reduction of the samples in the presence of Ni2+
cations. We have reported earlier [20] that Ti4+ cation was stable in
H2 up to 1000 ◦C in Cr and Fe substituted In2TiO5 samples. As such,
to obtain the TPR profiles of some simple oxides, TiO2 and Cr2O3,
are difficult because the standard approximate free energy change
(ꢂG◦ in KJ/mol) for the process: MO + H2 → metal + H2O are respec-
tively ∼220 and ∼140 [21]. However for In2(1−x)Ni2xTiO5−ı samples,
in addition to the normal nucleation and growth process, during
reduction the presence of Ni2+ in even a minor amount modifies
the reduction. Ni metal initially formed by reduction dissociates
and activates hydrogen. This hydrogen then reacts and reduces
the oxide (even Ti4+). This phenomenon is termed as hydrogen
spillover. In oxide catalysts the presence of metal cations, which
Table 3
H2 consumption data of In2(1−x) NixTiO5−ı samples obtained from the first TPR cycle
in temperature range of 25–1100 ◦C.
Sample
Calculated Experimentalb
Residue as identified by XRD
In0 andTiO2 rutile
compositiona
In2TiO5
In1.95Ni0.05TiO5−ı 8396
In1.9Ni0.1TiO5−ı
In1.8Ni0.2TiO5−ı
In1.7Ni0.3TiO5−ı
In1.6Ni0.4TiO5−ı
8390
8404
9009
8401
8412
8424
8436
8358
9528
In, TiO2 and ıIn3Ni2
10,514
10,153c
In, TiO2, ıIn3Ni2 and Ti2Ni
a
Stoichiometry determines ı as x.
TCD signal for manual injection of standard hydrogen has been used for calibra-
b
tion to find out the H2 consumption.
c
The difference observed in experimental values (higher) of H2 consumed as com-
pared to calculated values is attributed to reduction of Ti4+ metal ions to Ti metal
driven by presence of Ni2+ ions.