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Pd/SiC催化乙炔选择性加氢反应性能及构效研究OA

Performance and structure-activity relationship of Pd/SiC catalyst in selective hydrogenation of acetylene

中文摘要英文摘要

以高导热性SiC为载体,通过溶胶固定法制备了催化剂Pd/SiC,并将其应用于乙炔选择性加氢反应中.采用HRTEM,CO-FTIR,XRD,XPS等表征方法及计算流体力学(CFD)模拟仿真对所制备的Pd/SiC的构效关系进行研究.实验结果表明,与常用的Pd/Al2O3 相比,Pd/SiC具有较高的本征活性(转化频率为0.029 6 s-1)、较高的乙烯选择性(乙炔转化率92%,乙烯选择性73%)及较好的抗烧结能力.表征结果显示,高活性归因于较高的Pd分散度,高选择性归因于较高的Pd电子云密度.CFD 模拟结果表明,Pd/SiC 优异的导热性能够有效抑制催化剂床层表面温度升高,从而提高了催化剂的抗烧结能力.

The Pd/SiC catalyst,with high-thermal-conductivity SiC as the support,was prepared by the sol-immobilization method and applied in selective hydrogenation of acetylene.The structure-property relationship of the prepared Pd/SiC catalyst was investigated using characterization methods such as HRTEM,CO-FTIR,XRD,and XPS,as well as computational fluid dynamics(CFD)simulation.The experimental results show that compared with the commonly used Pd/Al2O3,Pd/SiC exhibits higher intrinsic activity(the conversion frequency of 0.029 6 s-1),higher ethylene selectivity(conversion of 92%with selectivity of 73%),and better sintering resistance.The characterization results indicate that the high activity is attributed to the higher Pd dispersion,while the high selectivity stems from the higher electron density of Pd.CFD simulation analysis reveals that the excellent thermal conductivity of Pd/SiC can effectively suppress the temperature rise of the catalyst bed,thereby enhancing the sintering resistance of the catalyst.

杨甜星;魏子荣;贺宇飞

连云港职业技术学院 材料与化工学院,江苏 连云港 222006北京化工大学 化工资源有效利用全国重点实验室,北京 100029北京化工大学 化工资源有效利用全国重点实验室,北京 100029||衢州资源化工创新研究院,浙江 衢州 324000

化学化工

乙炔选择性加氢分散度电子云密度导热性

acetylene selective hydrogenationdispersionelectron densitythermal conductivity

《石油化工》 2026 (5)

660-666,7

国家重点研发计划青年科学家项目(2022YFA1506200)连云港市科技项目(JCYJ2402)2025年江苏高校"青蓝工程"优秀青年骨干教师培养项目国家自然科学基金项目(U23B20164).

10.3969/j.issn.1000-8144.2026.05.002

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