丁烷
催化作用
催化裂化
扩散
反应速率常数
开裂
化学
化学工程
壳体(结构)
材料科学
分析化学(期刊)
色谱法
物理化学
动力学
热力学
复合材料
有机化学
物理
工程类
量子力学
作者
Qingxin Yang,Yuming Li,Zhentao Chen,Linxie Hu,Zhenye Li,Yajun Wang,Zhen Zhao,Chunming Xu,Guiyuan Jiang
摘要
Abstract A series of core‐shell HZSM‐5@mesoSiO 2 with tunable shell thickness from 10 to 70 nm was prepared and studied for n ‐butane catalytic cracking. With introducing of SiO 2 shell, the catalytic performance of HZSM‐5@mesoSiO 2 was largely enhanced, and n ‐butane conversion rate per Al site reached to 2.43 min −1 over HZSM‐5@mesoSiO 2 (1:4) at 675°C which is nearly twice to that of HZSM‐5 (1.34 min −1 ). The diffusion property of n ‐butane over as‐prepared sample was quantified by measuring the diffusional time constants using zero length column chromatography technique (ZLC). Combining with chemical reaction kinetic analysis, the quantitative relationship between diffusion property and catalytic performance was effectively established for the first time in n ‐butane catalytic cracking. Positive linear correlation between diffusional time constant ( D / R 2 ) and n ‐butane conversion rate per Al site could be found, which confirms that diffusion enhancement by hierarchical structure is an effective strategy to improve the activity of HZSM‐5 in catalytic cracking.
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