L. Bedel et al. / Journal of Catalysis 235 (2005) 279–294
293
4. Conclusions
higher than that of the best catalyst of the previous series (y = 0
in the present work, CO conversion of 2% at 270 ◦C).
La(1−y)Co0.4Fe0.6O3−δ materials prepared by the thermal
decomposition of mixed La–Co–Fe propionates did not lead
to La-deficient perovskites, although single perovskite phases
were observed by XRD up to a La deficiency of 0.3. Mössbauer
spectroscopy revealed the presence of an Fe2O3 phase in addi-
tion to the perovskite. Magnetic measurements were in favor of
the iron oxide phase γ -Fe2O3 instead of α-Fe2O3. According to
both micrographs and EDX analysis, iron oxide particles were
too small to diffract X-rays. They were surrounded by a non-
cation-deficient perovskite phase. La(1−y)Co0.4Fe0.6O3−δ ma-
terials thus may be considered nano-composites. The very small
size of some γ -Fe2O3 particles made the saturation of their
magnetization difficult to reach. However, these composites al-
ready exhibited very strong coercive fields (around 8500 Oe at
4 K). Even when Co-rich (e.g., LaCo0.73Fe0.27O3 for y = 0.2),
the perovskite-type phase crystallized in the cubic system. This
unexpected feature of LaCoxFe(1−x)O3 perovskite series being
either orthorhombic for x < 0.5 or rhombohedral for x ꢀ 0.5
can be explained by an epitaxial growth of the perovskite phase
over nanosize cubic γ -Fe2O3 cores.
References
[1] L.J. Tejuca, J.L.G. Fierro, Properties and Applications of Perovskite Type
Oxides, Dekker, New York, 1993.
[2] M.A. Peña, J.L.G. Fierro, Chem. Rev. 101 (2001) 1981.
[3] S. Lee, K.S. Lee, S.K. Woo, J.W. Kim, T. Ishihara, D.K. Kim, Solid State
Ionics 158 (3–4) (2003) 287.
[4] B.T. Cong, P.N. Anh Huy, N.H. Long, J. Magn. Magn. Mater. 262 (3)
(2003) 437.
[5] H. Arai, T. Yamada, K. Eguchi, T. Seiyama, Appl. Catal. 26 (1986) 265.
[6] T. Nitadori, M. Misono, J. Catal. 93 (1985) 93.
[7] K.S. Chan, J. Ma, S. Jaenicke, G.K. Chuah, Appl. Catal. A 107 (1994)
337.
[8] R. Doshi, C.B. Alcock, J.J. Carberry, Catal. Lett. 18 (1993).
[9] C. Petit, A. Kiennemann, P. Chaumette, O. Clause, French Patent 92/
11638 (1992).
[10] J.O. Pentuchi, M.A. Ulla, J.A. Marcos, E.A. Lombardo, J. Catal. 70 (1981)
1787.
[11] L. Wachowski, S. Zielinski, A. Burewicz, Acta Chim. Sci. Hung. 106
(1981) 217.
[12] L. Bedel, A.C. Roger, C. Estournès, A. Kiennemann, Catal. Today 85
(2003) 207.
The study of the reducibility of these composite oxides
showed that the γ -Fe2O3 nanocores were reducible at 450 ◦C
under hydrogen. This partial reduction gives rise to a metal
phase, the composition of which depends on the initial calcina-
tion temperature of the material (i.e., Co0.5Fe0.5 for the series
at 750 ◦C and Co0.6Fe0.4 for y = 0.4 at 900 ◦C). The cobalt
cations extracted from the cubic perovskite by reduction are re-
placed by iron cations of the Fe2O3 phase, and the oxide struc-
ture then is not destroyed by reduction. The amount of metal
alloy was directly related to the initial lanthanum deficiency
(i.e., increases with increasing y) and increased with increas-
ing initial calcination temperature of the oxides (10.9 wt% for
y = 0.4 at 750 ◦C and 14.1 wt% for y = 0.4 at 900 ◦C). The
increase in calcination temperature came with an increase in
metal particle size (10 nm for y = 0.4 at 750 ◦C and 28 nm for
y = 0.4 at 900 ◦C).
[13] J.W. Stevenson, T.R. Armstrong, L.R. Pederson, J. Li, C.A. Lewinshon,
S. Baskaran, Solid State Ionics 113–115 (1998) 571.
[14] D. Waller, J.A. Lane, J.A. Kilner, B.C.H. Steele, Solid State Ionics 86–88
(1996) 767.
[15] F.W. Poulsen, Solid State Ionics 129 (2000) 145.
[16] G.Ch. Kostogloudis, Ch. Ftikos, Solid State Ionics 126 (1999) 143.
[17] V.V. Kharton, A.P. Viskup, E.N. Naumovich, A.A. Tonoyan, O.P. Reut,
Mater. Res. Bull. 33 (7) (1998) 1087.
[18] A.R. Chakhmouradian, R.H. Mitchell, P.C. Burns, J. Alloys Compd. 307
(2000) 149.
[19] A.C. Roger, C. Petit, A. Kiennemann, J. Catal. 167 (1997) 447.
[20] H. Provendier, C. Petit, J.L. Schmitt, A. Kiennemann, J. Mater. Sci. 34
(1999) 4121.
[21] M. Evain, U-Fit V 1.3 Institut des Matériaux de Nantes, 1992.
[22] G. Dezanneau, A. Sin, H. Roussel, M. Audier, H. Vincent, J. Solid State
Chem. 173 (1) (2003) 216.
[23] P. Poix, Bull. Soc. Ceram. 72 (1966) 1.
[24] V.C. Belessi, T.V. Bakas, C.N. Costa, A.M. Efstathiou, P.J. Pomonis, Appl.
Catal. B 28 (2000) 13.
[25] V.C. Belessi, P.N. Trikalitis, A.K. Lavados, T.V. Bakas, P.J. Pomonis,
Appl. Catal. A 177 (1999) 53.
[26] J.G. Stevens, A.M. Khasanov, J.W. Miller, H. Pollak, Z. Li (Eds.), Möss-
bauer Mineral Handbook, Mössbauer Effect Data Center, 1998.
[27] J. Kaczér, T. Shalnikova, in: International Conference on Magnetism, Not-
tingham, 1964.
[28] O. Jarjayes, P.H. Fries, G. Bidan, J. Magn. Magn. Mater. 137 (1994) 205.
[29] L. Bedel, A.C. Roger, C. Estournès, A. Kiennemann, in: Proceedings of
9th International Symposium on Heterogeneous Catalysis, Varna, 2000,
p. 519.
[30] Powder Diffraction File, International Center for Diffraction Data, File
48-1818.
[31] W.C. Ellis, E.S. Greiner, Trans. Am. Soc. Met. 29 (1941) 415.
[32] Landolt Börstein—New Series III/19a 189.
[33] Landolt Börstein—New Series III/19a 157.
[34] P. Chaumette, P. Courty, A. Kiennemann, B. Ernst, Top. Catal. 2 (1995)
117.
Fischer–Tropsch activity is directly related to the amount of
metal alloy generated by partial reduction. Thus, the activity
increases with increasing lanthanum deficiency, that is, with an
increasing amount of γ -Fe2O3 nanocores in the fresh oxide. For
a similar lanthanum deficiency, the increasing amount of metal
with increasing initial calcination temperature has no beneficial
effect on catalytic activity, because of the concomitant enlarge-
ment of the alloy particle size.
The most deficient catalyst (y = 0.4) exhibited excellent C2–
C4 olefin selectivity. The decreased reaction temperature with
an increasing amount of metal led to diminished secondary
reactions of olefin readsorption and their consecutive hydro-
genation. The catalysts exhibited high stability under testing for
300 h.
The aim of improving catalytic activity by increasing the
amount of metal extractable by reduction with lanthanum de-
ficiency, without generating any real A-site deficiency, was
achieved. This is because the activity of the best catalyst of this
series (y = 0.4, CO conversion of 21% at 255 ◦C) was much
[35] J.B. Butt, T.-A. Lin, L.H. Schwartz, J. Catal. 97 (1986) 261.
[36] H. Schulz, M. Claeys, Appl. Catal. A 186 (1999) 109.
[37] J. Patzlaff, Y. Liu, C. Graffmann, J. Gaube, Appl. Catal. A 186 (1999) 145.
[38] A.A. Chen, M. Kaminsky, G.L. Geoffroy, M.A. Vannice, J. Phys. Chem.
90 (1986) 4810.