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Methanol steam reforming (MSR) catalysts are derived from perovskite-type oxides LaCo1-x-yPdxZnyO3 +/-delta by reductive pretreatment. The unsubstituted LaCoO3 +/-delta (LCO) and LaCo1-x-yPdxZnyO3 +/-delta (Co substituted with Pd and/or Zn) are synthesized by a citrate method and characterized by different techniques. The perovskite-type oxides exhibit a rhombohedral crystal structure and a comparable surface area (approximate to 8.5 (+/- 2) m(2) g(-1)). The temperature-programmed reduction (TPR) shows low (100 degrees C < T < 450 degrees C) and high (T > 450 degrees C) temperature reduction events that correspond to partial and complete reduction of the non-rareearth metal ions, respectively. At high temperatures, Pd-Zn alloy nanoparticles are formed exclusively on Pd-and Zn-containing LaCo1-x-yPdxZnyO3 +/-delta, as evident from high angular annular dark-field scanning transmission electron microscopy (HAADF-STEM). The CO2-selective MSR performance of the catalysts strongly depends on the reductive pretreatment temperature, catalyst composition (i.e., the Pd : Zn molar ratio and the degree of Co substitution) and reaction temperature. Only LaCo1-x-yPdxZnyO3 +/-delta catalysts show a low-temperature CO2 selectivity maximum between 225 and 250 degrees C, while all catalysts present similar high-temperature selectivity maxima at T > 400 degrees C. The former is missing on LCO, LaCo1-xPdxO3 +/-delta or LaCo1-yZnyO3 +/-delta. Pd-Zn nanoparticles facilitate Zn(OH)(2) and Co(OH)(2) formation exclusively on LaCo1-x-yPdxZnyO3 +/-delta, as evident from in situ XRD under steam atmosphere. This indicates the important role of Pd-Zn nanoparticles in the low-temperature CO2 selectivity, which is improved from 0 to 76% at 225 degrees C on LCO and LaCo0.75Pd0.125Zn0.125O3 +/-delta, respectively. The high-temperature CO2 selectivity is governed by the bulk catalyst composition and the occurrence of reverse water gas shift reaction

Methanol steam reforming catalysts derived by reduction of perovskite-type oxides LaCo1−x−yPdxZnyO3±δ

Methanol steam reforming catalysts derived by reduction of perovskite-type oxides LaCo_1−x−yPd_xZn_yO_3±δ