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Catalytic Transfer Hydrogenation of Furfural over Co3O4-Al2O3 Hydrotalcite-derived Catalyst

机译:Co3O4-Al2O3水滑石衍生催化剂催化转移糠醛糠醛

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摘要

The hydrogenation of furfural by catalytic hydrogen transfer to produce furfuryl alcohol has been investigated over a series of mixed oxides derived from hydrotalcite catalysts. Three different catalysts containing Ni, Co and Zn phases on an Al-rich amorphous support were synthesized and characterised. The catalytic performances were evaluated in a batch stirred reactor using 2-propanol as a solvent and hydrogen donor, with Co3O4-Al2O3 showing the highest activity and selectivity to FA (74 % yield; 97 % selectivity). The effects of temperature (T=120-180 degrees C) and reaction time (t=30 min-24 h) were also studied, reaching a FA maximum yield of 92 % at 150 degrees C after 24 h. The Co3O4-Al2O3 catalyst showed a loss of activity after the first run, which can be easily restored by a simple calcination treatment. The results establish a catalytic route to produce valuable furfuryl alcohol over 3d-transition metal-based catalysts without any external hydrogen supply.
机译:通过催化氢转移氢化糠醛在衍生自水滑石催化剂的一系列混合氧化物上研究了催化氢转移以产生糠醇。 合成含有Ni,Co和Zn相的三种不同的催化剂在富含族无定形载体上进行合成和表征。 使用2-丙醇作为溶剂和氢气供体在分批搅拌的反应器中评价催化性能,CO 3 O 4-Al 2 O 3显示出最高的活性和对Fa的选择性(74%收率; 97%的选择性)。 研究了温度(T = 120-180℃)和反应时间(T = 30 min-24h)的影响,在24小时后在150℃下达到92%的FA最大收率。 Co3O4-Al2O3催化剂在第一次运行后显示出活性损失,这可以通过简单的煅烧处理容易地恢复。 结果建立了在没有任何外部氢气供应的3D过渡金属基催化剂上生产有价值的糠醇的催化途径。

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