<p>CO esterification to dimethyl oxalate (DMO) plays a vital role in transforming inorganic C1 into organic oxygenated compounds. While Palladium (Pd)-based alumina catalysts exhibit excellent performance in this reaction, the regulation of active sites by alumina supports remains underexplored. To address this, two common types of alumina were used as supports for Pd-based catalysts prepared via the deposition-precipitation method. Notably, Pd nanoparticles (NPs)’ size was similar on both alumina supports, and the catalysts showed similar catalytic performance. The effect of calcination temperature was investigated: as the calcination temperature increased, the performance of the Pd/γ-Al<sub>2</sub>O<sub>3</sub> catalyst gradually decreased, whereas that of the Pd/α-Al<sub>2</sub>O<sub>3</sub> catalyst initially increased and then decreased. Further characterization confirmed that 1Pd-500/α-Al<sub>2</sub>O<sub>3</sub> exhibited the more hollow CO on Pd, which corresponded to the better catalytic performance. Overall, this study illustrates that selecting a suitable alumina as the support and proper calcination temperature can cause Pd NPs having edge sites at a higher fraction for more hollow CO and improve catalytic performance of CO esterification to DMO.</p> Graphical Abstract <p></p>

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Boosting CO Oxidative Esterification to Dimethyl Oxalate by the Regulation of Surface Pd Species on Aluminum Oxide

  • Qiuyue Mao,
  • Chen Zhang,
  • Yuanyuan Huang,
  • Yuan-Gen Yao

摘要

CO esterification to dimethyl oxalate (DMO) plays a vital role in transforming inorganic C1 into organic oxygenated compounds. While Palladium (Pd)-based alumina catalysts exhibit excellent performance in this reaction, the regulation of active sites by alumina supports remains underexplored. To address this, two common types of alumina were used as supports for Pd-based catalysts prepared via the deposition-precipitation method. Notably, Pd nanoparticles (NPs)’ size was similar on both alumina supports, and the catalysts showed similar catalytic performance. The effect of calcination temperature was investigated: as the calcination temperature increased, the performance of the Pd/γ-Al2O3 catalyst gradually decreased, whereas that of the Pd/α-Al2O3 catalyst initially increased and then decreased. Further characterization confirmed that 1Pd-500/α-Al2O3 exhibited the more hollow CO on Pd, which corresponded to the better catalytic performance. Overall, this study illustrates that selecting a suitable alumina as the support and proper calcination temperature can cause Pd NPs having edge sites at a higher fraction for more hollow CO and improve catalytic performance of CO esterification to DMO.

Graphical Abstract