Methanol steam reforming catalysts derived by reduction of perovskite-type oxides LaCo 1−x−y Pd x Zn y O 3±δ

Methanol steam reforming (MSR) catalysts are derived from perovskite-type oxides LaCo 1−x−y Pd x Zn y O 3±δ by reductive pretreatment. The unsubstituted LaCoO 3±δ (LCO) and LaCo 1−x−y Pd x Zn y O 3±δ (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 (≈8.5 (±2) m 2 g −1 ). The temperature-programmed reduction (TPR) shows low (100 °C < T < 450 °C) and high ( T > 450 °C) temperature reduction events that correspond to partial and complete reduction of the non-rare-earth metal ions, respectively. At high temperatures, Pd–Zn alloy nanoparticles are formed exclusively on Pd- and Zn-containing LaCo 1−x−y Pd x Zn y O 3±δ , as evident from high angular annular dark-field scanning transmission electron microscopy (HAADF-STEM). The CO 2 -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 LaCo 1−x−y Pd x Zn y O 3±δ catalysts show a low-temperature CO 2 selectivity maximum between 225 and 250 °C, while all catalysts present similar high-temperature selectivity maxima at T > 400 °C. The former is missing on LCO, LaCo 1−x Pd x O 3±δ or LaCo 1−y Zn y O 3±δ . Pd–Zn nanoparticles facilitate Zn(OH) 2 and Co(OH) 2 formation exclusively on LaCo 1−x−y Pd x Zn y O 3±δ , as evident from in situ XRD under steam atmosphere. This indicates the important role of Pd–Zn nanoparticles in the low-temperature CO 2 selectivity, which is improved from 0 to 76% at 225 °C on LCO and LaCo 0.75 Pd 0.125 Zn 0.125 O 3±δ , respectively. The high-temperature CO 2 selectivity is governed by the bulk catalyst composition and the occurrence of reverse water gas shift reaction.