Selective hydrogenation of γ-valerolactone to 1,4-pentanediol over hydrotalcite-derived CuCoAl catalysts

IF 7.2 2区 工程技术 Q1 CHEMISTRY, APPLIED Fuel Processing Technology Pub Date : 2024-02-29 DOI:10.1016/j.fuproc.2024.108068
Jiebang Peng , Donghong Zhang , Xin Tian , Mingyue Ding
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Abstract

In this study, a series of CuCoAl catalysts with different Cu/Co molar ratios were prepared from hydrotalcite-like precursors and then adopted for γ-valerolactone (GVL) hydrogenation to 1,4-pentanediol (1,4-PeD). By tuning the Cu/Co ratio in the CuCoAl catalysts and optimizing the reaction conditions, nearly 100% yield of 1,4-PeD was finally achieved with the Cu0.2Co0.8Al catalyst (Cu/Co = 1: 4) at 433 K and 4 MPa H2. The high activity of the Cu0.2Co0.8Al catalyst was attributed to the existence of Cu-CoOx synergistic active sites and the abundant surface acidity. The electron transfer from Cu to Co resulted in the formation oxygen-defected CoOx sites and surface acidic sites, which were beneficial for the adsorption of GVL and the activation of C-O/C=O bonds. The proximity between Cu particles and defective CoOx facilitated the dissociative adsorption of H2 on Cu0 and the subsequent hydrogen spillover to CoOx sites, thereby significantly promoted the selective hydrogenation of GVL to 1,4-PeD. In addition, applications of the Cu0.2Co0.8Al catalyst to the ring-opening reactions of other lactones (including α-adamyllactone, γ-caprolactone, δ-pentyllactone, and ε-caprolactone) were further investigated. Eventually, high yields (> 93%) of the corresponding diols were attained, demonstrating the excellent catalytic versatility of Cu0.2Co0.8Al in selective hydrogenation of lactones. Overall, this work shows high potential of hydrotalcite-derived CuCoAl catalysts for selective hydrogenation of GVL to 1,4-PeD, and provides insights for the design of efficient bimetallic catalysts in lactone hydrogenolysis.

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在衍生自氢化talcite的铜钴铝催化剂上将γ-戊内酯选择性氢化为 1,4-戊二醇
本研究以类氢滑石前驱体为原料,制备了一系列不同 Cu/Co 摩尔比的 CuCoAl 催化剂,并将其用于γ-戊内酯(GVL)加氢制 1,4-戊二醇(1,4-PeD)。通过调整 CuCoAl 催化剂中的 Cu/Co 比率和优化反应条件,最终在 433 K 和 4 MPa H2 条件下,Cu0.2Co0.8Al 催化剂(Cu/Co = 1:4)实现了近 100%的 1,4-PeD 收率。Cu0.2Co0.8Al 催化剂的高活性归功于 Cu-CoOx 协同活性位点的存在和丰富的表面酸性。电子从 Cu 转移到 Co 后形成了氧缺陷 CoOx 位点和表面酸性位点,这有利于 GVL 的吸附和 C-O/C=O 键的活化。Cu 颗粒和缺陷 CoOx 之间的接近有利于 H2 在 Cu0 上的离解吸附以及随后氢向 CoOx 位点的溢出,从而显著促进了 GVL 向 1,4-PeD 的选择性氢化。此外,还进一步研究了 Cu0.2Co0.8Al 催化剂在其他内酯(包括 α-金刚烷内酯、γ-己内酯、δ-戊内酯和 ε-己内酯)开环反应中的应用。最终,获得了相应二元醇的高产率(93%),证明了 Cu0.2Co0.8Al 在选择性氢化内酯方面的卓越催化多功能性。总之,这项工作显示了氢铝酸盐衍生的 CuCoAl 催化剂在选择性氢化 GVL 到 1,4-PeD 中的巨大潜力,并为设计内酯氢解中的高效双金属催化剂提供了启示。
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来源期刊
Fuel Processing Technology
Fuel Processing Technology 工程技术-工程:化工
CiteScore
13.20
自引率
9.30%
发文量
398
审稿时长
26 days
期刊介绍: Fuel Processing Technology (FPT) deals with the scientific and technological aspects of converting fossil and renewable resources to clean fuels, value-added chemicals, fuel-related advanced carbon materials and by-products. In addition to the traditional non-nuclear fossil fuels, biomass and wastes, papers on the integration of renewables such as solar and wind energy and energy storage into the fuel processing processes, as well as papers on the production and conversion of non-carbon-containing fuels such as hydrogen and ammonia, are also welcome. While chemical conversion is emphasized, papers on advanced physical conversion processes are also considered for publication in FPT. Papers on the fundamental aspects of fuel structure and properties will also be considered.
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