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Higher Acetone Conversion Obtained Over a TiO2-Pd Bifunctional Catalyst for Liquid-Phase Synthesis of Methyl Isobutyl Ketone: The Role of Al2O3 Support

机译:通过TiO2-Pd双官能催化剂获得更高的丙酮转化用于液相合成甲基异丁基酮的液相合成:Al2O3载体的作用

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摘要

We reported a bifunctional catalyst TiO2/Al2O3 and Pd/Cor for one-pot liquid-phase synthesis of MIBK from acetone in this paper. The characterizations of FT-IR, Raman spectra, TEM, XPS, CO2-TPD, NH3-TPD, Py-IR and TGA spectra revealed that the TiO2/Al2O3 could possess more acid sites and especially Lewis acid sites due to the coexistence of TiO2 and Al2O3. So a higher acetone conversion 35-45% at 150 degrees C and 2.0MPa pressure was achieved than ever reported for MIBK liquid-phase synthesis. In addition, the catalyst could keep active for at least 90h on stream at 80-90% MIBK selectivity. The phenomenon of carbonaceous accumulation on TiO2/Al2O leaded to the deactivation of catalyst.Graphic AbstractBecause of the coexistence of TiO2 and Al2O3. TiO2/Al2O3 could have more acid sites and especially Lewis acid sites. For liquid-phase synthesis of methyl isobutyl ketone, bifunctional catalyst TiO2/Al2O3&Pd/Cor showed higher acetone conversion.
机译:我们报道了一种双官能催化剂TiO2 / Al2O3和PD / Cor,用于本文的丙酮的丙酮的单罐液相合成MIBK。 FT-IR,拉曼光谱,TEM,XPS,CO2-TPD,NH3-TPD,PY-IR和TGA光谱的特征表明,TiO2 / Al2O3由于TiO 2的共存而具有更多的酸性位点和尤其是路易斯酸部位 和Al2O3。 因此,对于MIBK液相合成,迄今为止,实现了150℃和2.0MPa压力的丙酮转化35-45%。 此外,催化剂可以在80-90%的MIBK选择性上保持活性物流至少90小时。 TiO2 / Al2O上的碳质积累现象率引起了催化剂的失活。TiO2和Al2O3共存的摘要备注。 TiO2 / Al2O3可具有更多的酸性位点和尤其是路易斯酸性位点。 对于甲基异丁基酮的液相合成,双官能催化剂TiO2 / Al 2 O 3&Pd / Cor显示出更高的丙酮转化。

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