4.6 Article

Carbonic Anhydrase-Mimicking Keplerate Cluster Encapsulated Iron Trimesate for Base-Free CO2 Hydrogenation

Journal

ACS SUSTAINABLE CHEMISTRY & ENGINEERING
Volume 9, Issue 42, Pages 14051-14060

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acssuschemeng.1c03429

Keywords

Carbon dioxide; Hydrogenation; Formic acid; Mo-132 cluster; Metal-organic frameworks

Funding

  1. National Research Foundation of Korea [2020M1A2A6079677]
  2. [KK2011-00]
  3. National Research Foundation of Korea [2020M1A2A6079677] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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This study demonstrates a dual catalyst system incorporating CO2 hydration and Pd/C catalysts to increase the yield of formic acid from base-free CO2 hydrogenation. The addition of a Mo-132 cluster significantly improves the FA yields and turnover numbers of Pd/C through a ligand exchange-derived CO2 hydration process. The Mo-132@MIL-100(Fe) catalyst not only showed higher turnover numbers compared to the Mo-132 cluster, but also remained separable and recyclable with Pd/C for consecutive reactions.
Producing formic acid (FA) via base-free CO2 hydrogenation suffers from low conversion efficiency because of the difficulty of activating CO2 and the low solubility of CO2 in neutral water. In this paper, we demonstrate a dual catalyst system, incorporating CO2 hydration and Pd/C catalysts to increase the FA yield from base-free CO2 hydrogenation for the first time. As the CO2 hydration catalyst, a carbonic anhydrase-mimicking Keplerate-type Mo-132 cluster was used, and its heterogenized catalyst (Mo-132@MIL-100(Fe)) was prepared by encapsulating in a mesoporous iron trimesate (MIL-100(Fe)) structure. Notably, the addition of a Mo-132 cluster greatly increased the FA yields and turnover numbers (TONs) of Pd/C by similar to 3.8x through a ligand exchange-derived CO2 hydration process, as confirmed by a NMR study. Mo-132@MIL-100(Fe) was not only separable and recycled along with Pd/C for consecutive reactions without leaching and notable loss of activity, but also showed 2.8x higher TON (1257) compared to the Mo-132 cluster (TON = 452) under the same reaction conditions. The present strategy is applicable to various catalytic reactions, especially in aqueous-phase CO2 conversion systems.

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