甲醇
催化作用
铟
选择性
材料科学
氧化物
丙胺
溶剂热合成
无机化学
傅里叶变换红外光谱
化学工程
核化学
化学
有机化学
冶金
胺气处理
工程类
作者
Pengjing Chen,Longang Tao,Jian Zhu,Guofeng Zhao,Ye Liu,Yong Lu
标识
DOI:10.1002/ente.201800747
摘要
Indium oxide is as a promising catalyst for the hydrogenation of CO 2 to methanol. Previous studies mainly focused on the cubic‐phase In 2 O 3 (C‐In 2 O 3 ), but the hexagonal‐phase In 2 O 3 (H‐In 2 O 3 ) with a corundum structure has been rarely studied because of the difficulty in its synthesis. Herein, the morphology‐controllable H‐In 2 O 3 in situ structured onto a thin‐felt Al 2 O 3 /Al‐fiber is prepared by a facile mixed solvothermal method. The amount of H‐In 2 O 3 is strongly dependent on the urea/In molar ratio during the mixed solvothermal synthesis. The optimal catalyst obtained at a urea/In ratio of 4.5 possesses the highest amounts of oxygen vacancy and strong basic site. Such catalyst achieves a turnover frequency of 47.8 h −1 (the number of CO 2 converted into methanol per oxygen vacancy site per hour) and is stable for at least 200 h, being capable of converting 4.4% CO 2 into methanol at a selectivity of 67.6% at 325 °C (or higher selectivity at the expense of conversion below 325 °C) with a methanol space time yield of 0.20 g MeOH g cat −1 h −1 . In contrast, the microfibrous‐structured C‐In 2 O 3 (prepared by the incipient wetness impregnation method) delivers a very low methanol selectivity of only 36.8% under identical reaction conditions. In situ Fourier transform infrared spectroscopy experiments reveal that the H‐In 2 O 3 /Al 2 O 3 /Al‐fiber catalyzes CO 2 ‐to‐methanol conversion through formate intermediates.
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