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铜掺杂多孔金属氧化物上5-羟甲基糠醛向2,5-呋喃二甲醇和2,5-二甲基呋喃的可调谐选择性转化

Tunable and selective conversion of 5-HMF to 2,5-furandimethanol and 2,5-dimethylfuran over copper-doped porous metal oxides.

作者信息

Kumalaputri Angela J, Bottari Giovanni, Erne Petra M, Heeres Hero J, Barta Katalin

机构信息

Department of Chemical Engineering, University of Groningen, Nijenborgh 4, 9747 AG Groningen (The Netherlands); Department of Chemical Engineering, Parahyangan Catholic University, Ciumbuleuit 94, Bandung 40141 (West Java, Indonesia).

出版信息

ChemSusChem. 2014 Aug;7(8):2266-75. doi: 10.1002/cssc.201402095. Epub 2014 Jun 12.

Abstract

Tunable and selective hydrogenation of the platform chemical 5-hydroxymethylfurfural into valuable C6 building blocks and liquid fuel additives is achieved with copper-doped porous metal oxides in ethanol. A new catalyst composition with improved hydrogenation/hydrogenolysis activity is obtained by introducing small amounts of ruthenium dopant into the previously reported Cu(0.59) Mg2.34 Al1.00 structure. At a mild reaction temperature (100 °C), 2,5-furandimethanol is obtained with excellent selectivity up to >99%. Higher reaction temperatures (220 °C) favor selective deoxygenation to 2,5-dimethylfuran and minor product 2,5-dimethyltetrahydrofuran with a combined yield as high as 81%. Notably, these high product yields are maintained at a substrate concentration up to 10 wt% and a low catalyst loading. The influence of different alcohol solvents on product selectivity is explored. Furthermore, reaction intermediates formed at different reaction temperatures are identified. The composition of these product mixtures provides mechanistic insight into the nature of the reduction pathways that influence product selectivity. The catalysts are characterized by elemental analysis, TEM, and BET techniques before and after the reaction. Catalyst recycling experiments are conducted in batch and in a continuous-flow setup.

摘要

在乙醇中,使用铜掺杂的多孔金属氧化物实现了平台化学品5-羟甲基糠醛向有价值的C6结构单元和液体燃料添加剂的可调谐选择性氢化。通过将少量钌掺杂剂引入先前报道的Cu(0.59)Mg2.34Al1.00结构中,获得了具有改进的氢化/氢解活性的新型催化剂组合物。在温和的反应温度(100°C)下,2,5-呋喃二甲醇的选择性高达>99%。较高的反应温度(220°C)有利于选择性脱氧生成2,5-二甲基呋喃和少量产物2,5-二甲基四氢呋喃,总收率高达81%。值得注意的是,在底物浓度高达10 wt%和低催化剂负载量的情况下,仍能保持这些高产物收率。探索了不同醇溶剂对产物选择性的影响。此外,还鉴定了在不同反应温度下形成的反应中间体。这些产物混合物的组成提供了对影响产物选择性的还原途径本质的机理洞察。在反应前后,通过元素分析、透射电子显微镜(TEM)和比表面积测定(BET)技术对催化剂进行了表征。在间歇式和连续流动装置中进行了催化剂循环实验。

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