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超越甲酸生成的CO加氢制甲醇研究

Toward Methanol Production by CO Hydrogenation beyond Formic Acid Formation.

作者信息

Onishi Naoya, Himeda Yuichiro

机构信息

National Institute of Advanced Industrial Science and Technology, 16-1 Onogawa, Tsukuba, Ibaraki 305-8569, Japan.

Faculty of Pure and Applied Sciences, University of Tsukuba, Tsukuba, 1-1-1 Tennodai, Tsukuba, Ibaraki 305-8573, Japan.

出版信息

Acc Chem Res. 2024 Oct 1;57(19):2816-2825. doi: 10.1021/acs.accounts.4c00411. Epub 2024 Sep 16.

Abstract

ConspectusThe Paradigm shift in considering CO as an alternative carbon feedstock as opposed to a waste product has recently prompted intense research activities. The implementation of CO utilization may be achieved by designing highly efficient catalysts, exploring processes that minimize energy consumption and simplifying product purification and separation. Among possible target products derived from CO, methanol is highly valuable because it can be used in various chemical feedstocks and as a fuel. Although it is currently produced on a plant scale by heterogeneous catalysis using a Cu/ZnO-based catalyst, a limited theoretical conversion ratio at high reaction temperatures remains an issue. In addition, a catalytic system that can be adjusted to accommodate a variable renewable energy source for the synthesis of methanol is more desirable than current continuous-operation systems, which require a reliable energy supply. Recently, significant progress has been made in the field of homogeneous catalysis, which primarily relies on an indirect route to synthesize methanol via the hydrogenation of carbonate or formate derivatives in the presence of additives and solvents. However, homogeneous catalysis is inappropriate for industrial-scale methanol production because of the inefficient separation and purification processes involved.In this Account, we demonstrate a novel approach for methanol production under mild reaction conditions by CO hydrogenation catalyzed by multinuclear iridium complexes under heterogeneous gas-solid phase conditions without any additives and solvents. One of the aims of this Account provides insights for overcoming the barriers for efficient CO hydrogenation by focusing on catalyst design, specifically by incorporating varying functionalities into the ligand. The fundamental strategy entails activating hydrogen molecule and enhancing the hydricity of the resulting metal-hydride species, which is based on the following two concepts of catalyst design: (i) Activating a metal-hydride by electronic effects; and (ii) accelerating H heterolysis. We have elucidated the mechanism for accelerating H heterolysis using a state-of-the-art catalyst that contains an that responds to or participates in catalysis as opposed to a classical .We have also demonstrated a novel heterogeneous catalysis using a molecular catalyst as a key step for the hydrogenation of CO to methanol beyond formic acid formation. The dehydrogenation of formic acid as a reverse reaction of formic acid hydrogenation is strongly favored in acidic aqueous solution. To circumvent the equilibrium limitation, we have envisioned an alternative route that both prevents the liberation of formic acid into the reaction medium, and develops a multinuclear complex to facilitate the transfer of multiple reactive hydrides. The unconventional gas-solid phase catalysis is capable of preventing the liberation of formate species and promoting further hydrogenation of formic acid through multihydride transfer.This novel catalytic system, which is the fusion of a molecular catalyst in heterogeneous catalysis, provides high performance for methanol synthesis through a sophisticated catalyst design and straightforward separation processes. A detailed mechanistic analysis of molecular catalysts in the gas phase would lead to significant progress in the field of Surface Organometallic Chemistry (SOMC).

摘要

概述

将一氧化碳视为一种替代碳原料而非废弃物的范式转变,最近引发了大量的研究活动。一氧化碳利用的实现可以通过设计高效催化剂、探索能耗最小化的工艺以及简化产品的纯化和分离来达成。在源自一氧化碳的可能目标产物中,甲醇极具价值,因为它可用于多种化学原料并用作燃料。尽管目前甲醇是在工厂规模上通过使用基于铜/氧化锌的催化剂进行多相催化生产的,但在高反应温度下有限的理论转化率仍是一个问题。此外,一种能够进行调整以适应可变可再生能源来合成甲醇的催化系统,比当前需要可靠能源供应的连续运行系统更具优势。最近,均相催化领域取得了重大进展,该领域主要依靠在添加剂和溶剂存在下通过碳酸盐或甲酸盐衍生物的氢化间接合成甲醇的路线。然而,由于涉及低效的分离和纯化过程,均相催化不适用于工业规模的甲醇生产。

在本报告中,我们展示了一种在温和反应条件下通过多核铱配合物在非均相气 - 固条件下催化一氧化碳加氢来生产甲醇的新方法,且无需任何添加剂和溶剂。本报告的目的之一是通过关注催化剂设计,特别是通过将不同功能引入配体,为克服高效一氧化碳加氢的障碍提供见解。基本策略包括活化氢分子并增强所得金属氢化物物种的氢酸度,这基于以下两个催化剂设计概念:(i)通过电子效应活化金属氢化物;(ii)加速氢异裂。我们使用一种包含能响应或参与催化的[具体结构未给出,此处原文缺失]的先进催化剂阐明了加速氢异裂的机制,这与经典的[具体结构未给出,此处原文缺失]不同。

我们还展示了一种使用分子催化剂作为一氧化碳加氢生成甲醇而非仅生成甲酸的关键步骤的新型非均相催化。甲酸脱氢作为甲酸加氢的逆反应在酸性水溶液中强烈有利。为了规避平衡限制,我们设想了一条替代路线,既能防止甲酸释放到反应介质中,又能开发一种多核配合物以促进多个活性氢化物的转移。这种非常规的气 - 固相催化能够防止甲酸盐物种的释放,并通过多氢化物转移促进甲酸的进一步加氢。

这种新型催化系统是均相催化与非均相催化的融合,通过精密的催化剂设计和直接的分离过程,为甲醇合成提供了高性能。对气相中分子催化剂进行详细的机理分析将在表面有机金属化学(SOMC)领域取得重大进展。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/d09f/11447816/446d6c7ffbfa/ar4c00411_0002.jpg

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