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作 者:杨勇[1] 陶智超[1] 张成华[1] 王洪[1] 田磊[1] 徐元源[1] 相宏伟[1] 李永旺[1]
机构地区:[1]中国科学院山西煤炭化学研究所煤转化国家重点实验室,山西太原030001
出 处:《燃料化学学报》2004年第6期717-722,共6页Journal of Fuel Chemistry and Technology
基 金:国家高技术研究发展计划(863项目;2001AA523010);中国科学院知识创新重大工程项目(KGCX1 SW 02)。~~
摘 要:研究了焙烧温度对Fischer Tropsch(F T)合成Fe Mn催化剂的织构性质、还原行为以及在还原和反应过程中结构变化的影响;在H2 CO=2.0、260℃、2.5MPa和1000h-1条件下在固定床反应器上考察了焙烧温度对Fe Mn催化剂F T合成反应活性、烃产物选择性和运行稳定性的影响。XRD和TPR结果表明,随着焙烧温度的升高,催化剂中α Fe2O3晶粒增大,催化剂比表面积降低,促进Mn3+渗入α Fe2O3晶格中,形成了铁锰固溶体物相,使得催化剂难于还原,当焙烧温度升高到700℃时,催化剂中的α Mn2O3相完全消失。催化剂F T合成反应评价表明,在不降低催化剂活性的同时,焙烧温度的升高可显著地提高催化剂的反应运行稳定性,并促使烃产物分布向高碳数方向偏移;600℃焙烧的Fe Mn催化剂运行200h,总体活性高,失活速率较低,对低碳烯烃和中间馏分油段产物选择性好。The effects of calcination temperature on the textural properties, reduction behavior and structural change during reduction and reaction of the Fe-Mn Fischer-Tropsch synthesis catalyst were studied. The F-T performances of the catalysts calcinated at different temperatures were investigated in a fixed-bed reactor under the conditions of H_2/CO=2.0, 260?℃, 2.5?MPa and 1?000?h^(-1). The results of X-ray Diffraction and Temperature Programmed Reduction indicated that the increase of calcination temperature could increase the crystallite size of α-Fe_2O_3 and decrease the specific surface area of the catalysts. Mn^(3+) ion gradually incorporates into the crystal lattice of α-Fe_2O_3, and the reduction peak of α-Mn_2O_3 completely disappeares at 700?℃. This incorporation results in the formation of the stable Fe_2O_3-Mn_2O_3 solid solution phase, which restrains the reduction of the catalyst. It is found that the catalysts with different calcination temperatures show high initial activity, while the increase of calcination temperature could improve the stability of F-T activity and shift hydrocarbon products to higher molecular weight. The catalyst calcinated at 600?℃ shows relatively higher F-T activity and stability during the whole 200?h on stream of F-T run, which also gives the reasonable distribution of hydrocarbon and high selectivity of olefin and middle distilled cut.
关 键 词:F-T合成 FE-MN催化剂 焙烧温度 烃产物分布
分 类 号:TQ529.2[化学工程—煤化学工程]
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