稻壳灰为硅源合成Co/Ru/SBA-15催化剂在费托合成中的应用

J. J. Rodrigues, F. Fernandes, M. Rodrigues
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引用次数: 5

摘要

使用简单化合物的合成工艺变得有吸引力,因为它们为燃料生产提供了替代途径。钴基催化剂在Fischer - Tropsch法中具有广泛的适用性。研究了Co/Ru/SBA-15催化剂在Fischer - Tropsch合成中的应用。催化剂采用水热法合成的SBA-15分子筛,以稻壳灰为硅源,经过热处理和化学处理;同时,通过摩尔比为100Co/5Ru/139SiO2的湿浸渍方法加入金属。将催化剂在氮气和合成气流下进行热处理。在240℃、10 atm、H2:CO摩尔比为1 ~ 2的料浆床反应器中进行Fischer - Tropsch合成。采用x射线衍射- XRD、x射线能量分散- EDX、氮吸附等方法对SBA-15和催化剂进行了表征。用扫描电子显微镜(SEM)对SBA-15进行了表征,用程序升温还原(TPR)和透射电子显微镜(TEM)对催化剂进行了表征。SBA-15表现出典型的介孔材料形态痕迹,比面积较小,为627 m2/g。催化剂呈现出预先定义的组成,保持了结构,但浸渍后面积减少(339 m2/g)。利用RTP结果找到了氧化铁相的典型温度还原范围。在H2/CO摩尔比为1:1的条件下,催化剂对液态烃C5+的转化率高达88.20%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Co/Ru/SBA-15 CATALYSTS SYNTHESIZED WITH RICE HUSK ASHES AS SILICA SOURCE APPLIED IN THE FISCHER-TROPSCH SYNTHESIS
Synthesis processes using simple compounds become attractive as they offer alternative routes for fuel production. Cobalt-based catalysts have wide applicability in the Fischer Tropsch process. This work aims to evaluate the catalyst Co/Ru/SBA-15 in the Fischer Tropsch synthesis. The catalyst was prepared with the molecular sieve SBA-15 synthesized using the hydrothermal method with rice husk ashes, treated by heat and chemical processes, as silica source; and incorporating, simultaneously, metals by wet impregnation of molar ratio 100Co/5Ru/139SiO2. The catalyst was submitted to heat treatment under nitrogen and synthetic air flow. The Fischer Tropsch synthesis was carried out in a slurry bed reactor operating at 240oC, 10 atm, and H2:CO molar ratio raging between 1 and 2. The SBA-15 and the catalyst were characterized by X-ray diffraction- XRD, X-ray energy dispersion- EDX, and nitrogen adsorption. The SBA-15 was characterized using scanning electron microscopy- SEM, and the catalyst was characterized by temperature programmed reduction - TPR and transmission electron microscopy - TEM. SBA-15 showed typical morphology traces of mesoporous materials with a small specific area of 627 m2/g. The catalyst presented the pre-defined composition, maintaining the structure, but with area reduction after impregnation (339 m2/g). The ranges of temperature reduction typical of iron oxides phases were found using RTP results. The catalyst showed high conversion to liquid hydrocarbons C5+ (88.20%) in the molar ratio H2/CO of 1:1.
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