Kinetic study of selective hydrogenation of crotonaldehyde over Fe-promoted Ir/BN catalysts

Kinetic study of selective hydrogenation of crotonaldehyde over Fe-promoted Ir/BN catalysts
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Fe助剂Ir/BN催化剂上巴豆醛选择性加氢反应动力学研究

DOI:
10.1016/j.apsusc.2018.08.230
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发表时间:
2019
影响因子:
6.7
通讯作者:
Di Ji Qing
Di Ji Qing
中科院分区:
材料科学1区
文献类型:
--
作者:
Ning Xiang;Xu Yu Meng;Wu An Qi;Tang Cen;Jia Ai Ping;Luo Meng Fei;Di Ji Qing

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考察了一系列氧化铁改性的Ir/BN催化剂在巴豆醛气相选择加氢反应中的催化性能。加入的FeO xin的催化剂大大提高了性能,高达5倍的提高稳态巴豆醇产率(46.9%)相比,裸Ir/BN(7.2%)。表征结果表明,Ir-FeOx相互作用导致界面处产生新的活性位,从而提高了材料的性能.动力学研究表明,Ir/BN催化剂中Ir-FeOx界面活性位的转换频率(82.9 × 10−3s−1)远高于Ir 0-Irδ+位(3.10 × 10−3s−1),这是由于FeOx的促进导致了更高的本征速率常数(12.1 × 10−7v.s. 1.19× 10 - 7 molg-1 s-1)和较高的吸附平衡常数(3.49 v.s. 0.62 kPa−1)。
A series of FeOx-promoted Ir/BN catalysts were tested for gas phase selective hydrogenation of crotonaldehyde. The addition of FeOxin the catalyst greatly improves the performance, up to a 5-fold enhanced steady state crotyl alcohol yield (46.9%) compared to that of the bare Ir/BN (7.2%). The characterization results reveal that the Ir-FeOxinteraction results in the generation of new active sites at the interface, which are responsible for the enhanced performance. The kinetic study showed that the Ir-FeOxinterfacial active site has much higher turnover frequency (82.9 × 10−3s−1) than the Ir0-Irδ+site in the Ir/BN catalyst (3.10 × 10−3s−1), due to the promotion of FeOxleads to a higher intrinsic rate constant (12.1 × 10−7v.s. 1.19 × 10−7mol g−1s−1) and a higher adsorption equilibrium constant of crotonaldehyde (3.49 v.s. 0.62 kPa−1).
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