Optimizing the Interfacial Environment of Triphasic ZnO-Cu-ZrO2 Confined inside Mesoporous Silica Spheres for Enhancing CO2 Hydrogenation to Methanol

Achieving the desired catalytic activity and selectivity in CO 2 hydrogenation to methanol remains a grand challenge using nonprecious metals. Herein, the well-known ternary Cu-ZnO-ZrO 2 (CZZ) was spatially sequestered as fine, uniformly dispersed active interfaces onto an engineered mesoporous silica sphere (MSS), giving rise to Cu-ZnO-ZrO 2 /MSS (CZZ-MSS) with confined binary Cu-ZnO/Cu-ZrO 2 and ternary interfaces that fostered methanol production under moderate conditions (30 bar and 200–280 °C). By systematically investigating the CZZ-MSS performance, we show that spatial confinement and optimization of the interfacial environment of the catalytically active interfaces inside well-fabricated mesoporous silica deliver a markedly enhanced specific methanol yield (2211 g MEOH ·kg Cu –1 ·h –1 ) compared to conventional supported catalysts including an industrial catalyst (368 g MEOH ·kg Cu –1 ·h –1 ) and a vast majority of reported catalysts. Besides, the strong metal–support interaction arising from interacting metallic Cu and metal oxides (ZnO and ZrO 2 ) within the confined, ultrasmall nanoparticles (<3.0 nm) demotes the sintering of Cu NPs while retaining their H 2 dissociation strength, resulting in superior and prolonged catalytic stability over 100 h. In situ DRIFTS of confined catalysts with monophasic, biphasic, and triphasic interfaces expectedly suggests the occurrence of different CO 2 hydrogenation reaction paths over triphasic Cu-ZnO-ZrO 2 /MSS (formate pathway) compared to monophasic Cu/MSS (reverse water–gas shift (RWGS) pathway) and biphasic ZnO-ZrO 2 /MSS. From the appreciable insights gained herein, the rational support synthesis bringing the confinement effect to the robust ZnO-Cu-ZrO 2 interface is the rationale behind the higher rate of methanol synthesis observed in the CO 2 hydrogenation.