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Catalytic performance of KL zeolite-supported iron and cobalt catalysts for the Fischer-Tropsch synthesis

机译:用于费城托合成的KL沸石负载铁和钴催化剂的催化性能

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摘要

In this work, Fe and Co were introduced into a KL zeolite support by incipient wetness impregnation to obtain catalysts for the Fischer-Tropsch synthesis (FTS). The samples were analyzed by several techniques including atomic absorption spectroscopy (AAS), N-2 adsorption, X-ray diffraction (XRD), H-2-temperature programmed reduction (TPR) and transmission electron microscopy (TEM). The catalytic performance for the FTS was tested with a fixed bed reactor. The particle size distribution of the samples was estimated by TEM microphotographs and showed that the diameters of the iron and cobalt particles were similar to 6 nm and 8-20 nm, respectively. The catalyst with the higher percentage of iron promoted the highest CO conversion, and the distribution of the products was shifted to light fractions. The iron-based catalysts were more active than cobalt in the CO conversion, but the latter yielded a higher content of hydrocarbons with 5 and more carbons.
机译:在这项工作中,通过初期的湿度浸渍将Fe和Co引入KL沸石载体中,得到Fischer-Tropsch合成(FTS)的催化剂。 通过包括原子吸收光谱(AAS),N-2吸附,X射线衍射(XRD),H-2-温度编程的还原(TPR)和透射电子显微镜(TEM)的几种技术分析样品。 用固定床反应器测试FTS的催化性能。 通过TEM显微照片估计样品的粒度分布,并表明铁和钴颗粒的直径分别类似于6nm和8-20nm。 具有较高百分比的铁促进最高CO转化的催化剂,并将产物的分布移至轻质分数。 铁基催化剂比CO转化中的钴更活跃,但后者含有5种碳氢化合物的含量较高。

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