Selective hydrogenation of 1,3-butadiene to butenes on ceria-supported Pd, Ni and PdNi catalysts: Combined experimental and DFT outlook

Toyin Shittu , Aasif A. Dabbawala , Labeeb Ali , Abbas Khaleel , Muhammad Z. Iqbal , Dalaver H. Anjum , Kyriaki Polychronopoulou , Mohammednoor Altarawneh
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Abstract

The regulation of catalyst activity and selectivity using a reducible support for the industrially relevant hydrogenation of 1,3-butadiene to more valuable butene products was achieved. Supported palladium and nickel–palladium catalysts on ceria were prepared and characterized with hydrogen temperature programmed reduction (H2-TPR), hydrogen temperature programmed desorption (H2-TPD), X-ray photoelectron spectroscopy (XPS), high resolution transmission electron microscopy (HR-TEM), high-angle annular dark-field scanning transmission electron microscopy (HAADF-STEM), temperature programmed oxidation (TPO), energy dispersive spectroscopy (EDS), and N2 adsorption–desorption to examine their chemical and physical properties. Pathways guiding the reaction were determined using the density functional theory (DFT). H2-TPR confirmed that palladium oxide was reduced, and nickel oxide species strongly interacted with the CeO2 support. The Ce3+ concentration determined by XPS showed that all catalysts surface contained the Ce reduced state. The catalysts showed a similar BET surface area, with 4Pd–Ce presenting the lowest value due to particle aggregation, which was confirmed from the EDS mapping analysis. Butadiene conversion consistently increased with temperature (40 °C–120 °C) until full conversion was reached on all the Pd catalysts while the maximum conversion on the 4Ni-Ce catalyst was 88 % at 120 °C. Product distribution revealed that 4 % Pd content directed the products toward butane when 40 °C was exceeded. Constructed mechanisms by DFT calculations featured low reaction barriers for the involved surface hydrogenation steps, and thus, they accounted for the observed low temperature of the surface hydrogenation activity. Selective formation of 1-butene partially stemmed from its relatively weak binding to Ni sites in reference to Pd sites. The mapped-out mechanisms entailed a higher reaction barrier for the formation of 2-butene, in agreement with the experimental observation pertinent to its formation at higher temperatures when compared with that of 1-butene.

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在铈支撑的钯、镍和钯镍催化剂上将 1,3-丁二烯选择性氢化为丁烯:实验和 DFT 综合展望
在将 1,3-丁二烯加氢转化为更有价值的丁烯产品的工业相关过程中,使用可还原的载体实现了对催化剂活性和选择性的调节。制备了铈上的支撑钯和镍钯催化剂,并利用氢温度编程还原(H2-TPR)、氢温度编程解吸(H2-TPD)、X 射线光电子能谱(XPS)、高分辨率透射电子显微镜(HR-TEM)对其进行了表征、高角度环形暗场扫描透射电子显微镜 (HAADF-STEM)、温度编程氧化 (TPO)、能量色散光谱 (EDS) 和 N2 吸附-解吸等方法来检测它们的化学和物理特性。利用密度泛函理论(DFT)确定了指导反应的途径。H2-TPR 证实氧化钯被还原,氧化镍物种与 CeO2 支持物发生了强烈的相互作用。通过 XPS 测定的 Ce3+ 浓度表明,所有催化剂表面都含有还原态的 Ce。催化剂显示出相似的 BET 表面积,其中 4Pd-Ce 因颗粒聚集而显示出最低值,EDS 图谱分析也证实了这一点。丁二烯的转化率随着温度(40 ℃-120 ℃)的升高而不断提高,直至所有钯催化剂都达到完全转化,而 4Ni-Ce 催化剂在 120 ℃ 时的最大转化率为 88%。产物分布显示,当温度超过 40 °C 时,4% 的钯含量会将产物引向丁烷。通过 DFT 计算构建的机理显示,涉及表面氢化步骤的反应壁垒较低,因此,它们解释了所观察到的低温表面氢化活性。1-butene 的选择性形成部分源于其与镍位点的结合力相对钯位点较弱。所绘制的机理表明,与 1-丁烯相比,2-丁烯在更高温度下形成的反应障碍更高,这与实验观察结果一致。
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来源期刊
Materials Science for Energy Technologies
Materials Science for Energy Technologies Materials Science-Materials Science (miscellaneous)
CiteScore
16.50
自引率
0.00%
发文量
41
审稿时长
39 days
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