摘要
利用等体积浸渍法制备不同镁含量的Mg-Silicalite-1 (Mg-SC-1)分子筛,以该分子筛为载体负载Pt-Sn双金属组分催化异丁烷脱氢反应,采用固定床连续反应器评价催化剂性能,并利用X-射线粉末衍射(XRD)、N2吸附-脱附、程序升温还原(H2-TPR)、扫描电镜(SEM)和碳含量分析等方法研究不同MgO含量的Pt-Sn/Mg-SC-1催化剂的催化性能。实验结果表明,添加w(MgO)=7%到SC-1载体,再负载Pt-Sn组分制备的催化剂异丁烷脱氢效果较好,相比于以纯硅SC-1分子筛为载体的催化剂具有高的反应稳定性和活性。而且经Mg改性后的SC-1载体与助剂SnOx物种之间存在较强的相互作用,导致SnOx物种不易被还原,并促进Pt粒子的分散度。在反应12 h后含w(MgO)=7%的Pt-Sn/Mg-SC-1催化剂仍保留较多的活性Pt粒子。
Pt-Sn/Mg-SC-1 catalysts with different magnesium contents were prepared by sequential incipient wetness impregnation, which were evaluated in a micro fixed bed continuous reactor for isobutane dehydrogenation. X-ray powder diffraction(XRD), N2 adsorption-desorption, temperature programmed reduction(H2-TPR), scanning electron microscopy(SEM) and carbon content analysis were used to study the catalytic performance of the Pt-Sn/Mg-SC-1 catalysts. The experimental results indicate that the Pt-Sn/Mg-SC-1 catalyst with w(MgO) = 7% exhibits excellent dehydrogenation performance. The characterization results reveal that the interaction between Mg-SC-1 and SnOx species is enhanced, and the SnOx species are not easily reduced, which is beneficial to the dispersion of Pt particles. Moreover, the Pt-Sn/Mg-SC-1 catalysts with w(MgO) = 7% has more active Pt particles than other catalysts after 12 h reaction.
引文
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