An examination of dimethyl oxalate hydrogenation to methyl glycolate on silica-supported Ni–Co alloy catalysts†

Abstract

The selective hydrogenation of dimethyl oxalate (DMO) to methyl glycolate (MG) is becoming increasingly attractive for the industrial production of polyglycolic acid (PGA) biodegradable plastics. However, it is still necessary to develop highly selective/active and affordable DMO hydrogenation catalysts for the large-scale production of MG and PGA. In this report, silica-supported Ni–Co alloy catalysts were meticulously investigated for the selective hydrogenation of dimethyl oxalate to methyl glycolate. Compared with monometallic Ni or Co, the supported Ni–Co alloy catalysts with an appropriate doping of Co in Ni resulted in the significant promotion of dimethyl oxalate conversion and methyl glycolate selectivity at mild temperature (180 °C). Optimized dimethyl oxalate conversion and selectivity for methyl glycolate were 87% and 86%, respectively, on the 15Ni–10Co/SiO₂ catalyst. The promotion of dimethyl oxalate conversion was attributed to the large capacity and strong strength of hydrogen adsorption, as proven via H₂-TPD, and the active sites with uniform strength for CO adsorption and dimethyl oxalate (or key oxygenated intermediates) adsorption, as proven via in situ CO-DRIFTS. These phenomena were enhanced by the effective interaction between Ni and Co. Furthermore, it was found that the strength of acid sites has an influence on product selectivity control for ethanol and methyl formate; particularly, the synergy between the acid sites and metal sites may facilitate deep hydrogenation of dimethyl oxalate to form unexpected methyl formate. This study not only shows the catalytic behavior of dimethyl oxalate hydrogenation on non-precious Ni–Co alloy catalysts but also provides new insights into designing Ni-based catalysts for the selective hydrogenation of oxygenates with multiple ester groups.