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定制新型 Co-Co 双相纳米粒子用于选择性 CO 加氢制乙醇。

Tailored design of novel Co-Co dual phase nanoparticles for selective CO hydrogenation to ethanol.

机构信息

Department of Chemical Engineering, Institute of Chemical Technology, Nathalal Parekh Marg, Matunga 400019, Mumbai, India.

Department of Chemical Engineering, Institute of Chemical Technology, Nathalal Parekh Marg, Matunga 400019, Mumbai, India.

出版信息

J Environ Sci (China). 2025 Mar;149:598-615. doi: 10.1016/j.jes.2024.01.047. Epub 2024 Mar 7.

DOI:10.1016/j.jes.2024.01.047
PMID:39181671
Abstract

Catalytic hydrogenation of CO to ethanol is a promising solution to address the greenhouse gas (GHG) emissions, but many current catalysts face efficiency and cost challenges. Cobalt based catalysts are frequently examined due to their abundance, cost-efficiency, and effectiveness in the reaction, where managing the Co to Co ratio is essential. In this study, we adjusted support nature (AlO, MgO-MgAlO, and MgO) and reduction conditions to optimize this balance of Co to Co sites on the catalyst surface, enhancing ethanol production. The selectivity of ethanol reached 17.9% in a continuous flow fixed bed micro-reactor over 20 mol% Co@MgO-MgAlO (CoMgAl) catalyst at 270 °C and 3.0 MPa, when reduced at 400 °C for 8 h. Characterisation results coupled with activity analysis confirmed that mild reduction condition (400 °C, 10% H balance N, 8 h) with intermediate metal support interaction favoured the generation of partially reduced Co sites (Co and Co sites in single atom) over MgO-MgAlO surface, which promoted ethanol synthesis by coupling of dissociative (CHx*)/non-dissociative (CHxO*) intermediates, as confirmed by density functional theory analysis. Additionally, the CoMgAl, affordably prepared through the coprecipitation method, offers a potential alternative for CO hydrogenation to yield valuable chemicals.

摘要

CO 催化加氢制乙醇是解决温室气体 (GHG) 排放的一种很有前途的方法,但许多现有的催化剂都面临着效率和成本方面的挑战。钴基催化剂因其丰富的资源、成本效益以及在反应中的有效性而经常被研究,其中管理 Co 与 Co 的比例是至关重要的。在这项研究中,我们调整了载体性质(AlO、MgO-MgAlO 和 MgO)和还原条件,以优化催化剂表面上 Co 与 Co 位的平衡,从而提高乙醇的产量。在 270°C 和 3.0 MPa 条件下,在连续流动固定床微反应器中,20 mol% Co@MgO-MgAlO(CoMgAl)催化剂上的选择性达到了 17.9%,催化剂在 400°C 下还原 8 小时。通过对催化剂的特性分析,结合活性分析,我们发现温和的还原条件(400°C、10% H 平衡 N、8 h)与中等的金属载体相互作用有利于在 MgO-MgAlO 表面上生成部分还原的 Co 位(单原子中的 Co 和 Co 位),这通过密度泛函理论分析证实了有利于通过解离(CHx*)/非解离(CHxO*)中间体的偶联促进乙醇的合成。此外,通过共沉淀法制备的 CoMgAl 价格低廉,为 CO 加氢生成有价值的化学品提供了一种潜在的替代方法。

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