화학공학소재연구정보센터
Applied Catalysis A: General, Vol.252, No.2, 251-260, 2003
Investigations on the structural changes of two CO/SiO2 catalysts by performing Fischer-Tropsch synthesis
The structural changes of Co/SiO2 catalysts by performing FT synthesis were investigated, including the influences of cobalt particle sizes and of the reaction conditions, two CO/SiO2 catalysts were prepared by impregnation method with cobalt nitrate as precursor: the one, Co/SiO2(1), was prepared by direct reduction of SiO2-supported nitrate precursor in H-2 at 350degreesC using a slow temperature ramping protocol (0.2degreesC/min), and the other, CO/SiO2(2), was prepared by calcinations of the nitrate precursor in air at 450 degreesC, followed by H-2 reduction at 400 degreesC. The cobalt particles over these two catalysts are expected to be different in size. These two catalysts were used for Fr synthesis for 60h at 1.0MPa and 200-240degreesC. Both the reduced and used catalysts were characterized by XRD, extended X-ray absorption fine structure (EXAFS) and H-2 chemisorptions. The CO/SiO2(1) catalyst exhibits obviously higher activity for FT synthesis than the CO/SiO2(2) catalyst. However, on increasing reaction temperature from 200 to 240degreesC, the ratio of cobalt-time yield (moles CO converted/total atom cobalt-s) on the Co/SiO2(1) catalyst to that on the Co/SiO2(2) catalyst decreases from 2.7 to 1.9. Codegrees crystallites formed on the Co/SiO2(1) catalyst are significantly smaller than those on the CO/SiO2(2) catalyst, and Co dispersion of the Co/SiO2(1) catalyst is greatly higher than that of the Co/SiO2(2) catalyst. During FF synthesis, the Col crystallites only grow with short-range order, and no cobalt oxide is formed. But Co dispersions of the catalysts decrease significantly, which may result from the aggregation of the Col crystallites. As the reaction temperature increases from 200 to 240 degreesC, the small cobalt particles on the CO/SiO2(1) catalyst aggregate more significantly than the large cobalt particles on the CO/SiO2(2) catalyst. This is the main reason responsible for the significant decrease in the ratio of the cobalt-time yield on the Co/SiO2(1) catalyst to that on the CO/SiO2(2) catalyst. (C) 2003 Elsevier B.V. All rights reserved.