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Cation reducibility of LaNi0.5Ti0.5O3, LaNi0.5Ti0.45Co0.05O3, and LaNi0.45Co0.05Ti0.5O3 perovskites from X-ray powder diffraction data using the Rietveld method

Published online by Cambridge University Press:  11 May 2022

Mayra Guamán-Ayala
Affiliation:
Departamento de Energía y Mecánica, Carrera de Petroquímica, Universidad de las Fuerzas Armadas – ESPE, EC170501 Sangolquí, Ecuador
Pablo V. Tuza*
Affiliation:
Departamento de Energía y Mecánica, Carrera de Petroquímica, Universidad de las Fuerzas Armadas – ESPE, EC170501 Sangolquí, Ecuador
Mariana M. V. M. Souza
Affiliation:
Escola de Química, Universidade Federal do Rio de Janeiro (UFRJ), Centro de Tecnologia, Bloco E, Sala 206, CEP 21941-909, Rio de Janeiro/RJ, Brazil
*
a)Author to whom correspondence should be addressed. Electronic mail: pvtuza@espe.edu.ec

Abstract

In the present work, LaNi0.5Ti0.5O3, LaNi0.5Ti0.45Co0.05O3, and LaNi0.45Co0.05Ti0.5O3 perovskites were synthesized using the modified Pechini method. After reduction, the studied perovskites changed crystal structure from the perovskite crystal structure to a cubic symmetry, with space group $Pm\bar{3}m$. The reduction partially decomposed the samples to Ni0 (Co free perovskite), Ni0–Co0, La2O3, La2TiO5, and non-stoichiometric La2NiO4, depending on H2 content of the reductive gases. The degree of reduction of nickel from LaNi0.5Ti0.5O3 reduced with 1.8% H2/Ar and 10% H2/Ar was equal to 36.5% and 95.3%, respectively, while that from LaNi0.5Ti0.45Co0.05O3 or LaNi0.45Co0.05Ti0.5O3, including cobalt, reduced with 10% H2/Ar, was equal to 71.9% and 93.9%, respectively. LaNi0.5Ti0.45Co0.05O3 showed Ni3+ and Co3+ amounts higher than the other perovskites. By increasing H2 content in the reductive mixture from 1.8% to 10%, sintering of metallic nickel was not observed. Moreover, Ni0 displayed weaker metal–support interaction than that observed for Co0, where the support was composed of La containing oxides. LaNi0.5Ti0.5O3 perovskite was used as a catalyst for steam reforming of methane. Syngas production was attributed to the number of Ni sites determined using Rietveld Refinement of X-ray diffraction pattern of this catalyst after the reaction.

Information

Type
Technical Article
Copyright
Copyright © The Author(s), 2022. Published by Cambridge University Press on behalf of International Centre for Diffraction Data
Figure 0

TABLE I. Theoretical and experimental chemical compositions of as-synthesized materials.

Figure 1

Figure 1. Observed (black circles), calculated (red line), and difference (gray bottom line) XRD patterns for (a) LN0.5T0.5O-1.8, (b) LN0.5T0.5O-10, (c) LN0.5T0.45C0.05O-10, and (d) LN0.45C0.05T0.5O-10.

Figure 2

TABLE II. Reduction conditions, average crystallite size, phase analysis results, conventional discrepancy factors from Rietveld refinement of powder XRD data, H2 uptake, RD calculated using Rietveld Refinement (RDRR), and TPR (RDTPR) for LN0.5T0.5O-1.8, LN0.5T0.5O-10, LN0.5T0.45C0.05O-10, and LN0.45C0.05T0.5O-10.

Figure 3

Figure 2. H2 uptake (a) from room temperature to 1000 °C, along with (b) isothermal period equal to 45 min for the LN0.5T0.5O-1.8, and 330 min for LN0.5T0.5O-10, LN0.5T0.45C0.05O-10, and LN0.45C0.05T0.5O-10.

Figure 4

Figure 3. Methane conversion and syngas production from steam reforming using LN0.5T0.5O catalyst.

Figure 5

Figure 4. Observed (black circles), calculated (red line), and difference (gray bottom line) XRD patterns for LN0.5T0.5O after steam reforming of methane.

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