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首页> 外文期刊>Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications >Highly active iridium-rhenium catalyst condensed on silica support for hydrogenolysis of glycerol to 1,3-propanediol
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Highly active iridium-rhenium catalyst condensed on silica support for hydrogenolysis of glycerol to 1,3-propanediol

机译:高活性铱 - 铼催化剂凝结在二氧化硅载体上,用于甘油的氢化溶解至1,3-丙二醇

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Increase of loading amount of Ir-ReOx/SiO2 catalyst up to 20 wt% of Ir enhanced the Ir-based activity in glycerol hydrogenolysis to 1,3-propanediol. The ratio of used precursor amount was set constant (Re/Ir = 1; "nominal" Re/Ir ratio); however, actual Re/Ir amount was lower at higher loading amount because of the loss of Re during calcination. The catalytic performance, reactivity of related substrates and kinetics over optimized Ir-ReOx/SiO2 (20 wt%-Ir, Re/Ir = 0.34, actual) was compared with the previously reported catalyst (4 wt%-Ir, Re/Ir = 1, nominal; Re/Ir = 0.83, actual) without H2SO4 addition which increases the activity and stability of 4 wt%-Ir Ir-ReOx/SiO2 catalyst. High 1,3-propanediol selectivity (ca. 70%) was obtained over 20 wt%-Ir Ir-ReOx/SiO2 at 20% conversion level of glycerol. This high selectivity was almost independent of glycerol concentrations, while 4 wt%-Ir Ir-ReOx/SiO2 catalyst showed lower selectivity when glycerol concentration was lower. The 20 wt%-Ir Ir-ReOx/SiO2 exhibited good reusability under optimized reaction conditions when recovered without exposure to air. Small Ir metal particles ((similar to)3 nm) were observed from both XRD and TEM regardless of high Ir loading amount. The results of XANES and EXAFS suggested high reduction degree of Re species ((similar to)80%); however, further characterization of XRD and CO FT-IR supported the absence of Ir-Re alloy. Combined with TPR and CO adsorption results, we proposed that ReOx cluster at low average valence (ca. + 1(similar to) + 2) was attached to Ir metal. This unique structure decreased the effect of SiO2 support and increased the number of active sites, accounting for higher activity. The heterolytic dissociation of hydrogen molecule ((similar to) + 1 reaction order on H-2 pressure) and strong interaction between glycerol and catalyst surface ((similar to)0 reaction order on glycerol concentration around standard reaction conditions, 67 wt% glycerol solution) were suggested for 20 wt%-Ir Ir-ReOx/SiO(2 )catalyst. This 20 wt%-Ir Ir-ReOx/SiO2 catalyst can be also applied to various substrates with -O-C-CH2OH structure for the selective cleavage of the C-O bond.
机译:IR-Reox / SiO 2催化剂的加载量增加20wt%的IR增强了甘油氢解的IR基活性至1,3-丙二醇。使用的前体量的比例设定为恒定(RE / IR = 1;“标称”RE / IR比率);然而,由于在煅烧过程中失去Re的损失,实际RE / IR量较高。将优化的IR-Reox / SiO 2上的催化性能,相关底物和动力学的反应性与先前报道的催化剂(4wt%-Ir,Re / Ir = 1,标称; RE / IR = 0.83,实际)没有H2SO4添加,其增加4wt%-Ir Ir-Reox / SiO2催化剂的活性和稳定性。在20%重量的-IR-Reox / SiO 2下,在20%转化水平的甘油中获得高1,3-丙二醇选择性(约70%)。这种高选择性几乎依赖于甘油浓度,而当甘油浓度较低时,4wt%-r-Reox / SiO 2催化剂的选择性较低。 20wt%-Ir Ir-Reox / SiO2在恢复时在未暴露于空气时在优化的反应条件下表现出良好的可重用性。无论高IR负载量如何,从XRD和TEM都观察到小红外金属颗粒((类似于)3nm)。 Xanes和EXAFS的结果表明RE少量的缩减程度((类似于)80%);然而,XRD和CO FT-IR的进一步表征支持不存在IR-Re合金。结合TPR和CO吸附结果,我们提出将雷达簇在低平均值(约+ 1(类似于)+ 2)附着IR金属。这种独特的结构降低了SiO2支持的效果并增加了活性地点的数量,占较高活动的概率。氢分子的异解离子((类似于H-2压力的反应顺序)和甘油和催化剂表面之间的强相互作用((类似于)0反应顺序在标准反应条件下甘油浓度,67wt%甘油溶液提出了20wt%-Ir Ir-Reox / SiO(2)催化剂。该20wt%-Ir Ir-Reox / SiO 2催化剂也可以应用于具有-C-C-CH 2 OH结构的各种基材,用于选择性切割C-O键。

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