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Ni助剂FeMnK/SiO2费托合成催化剂的结构性质及还原碳化行为研究
  • 期刊名称:燃料化学学报, 2006, 34 (6):695-699
  • 时间:0
  • 分类:TQ529.2[化学工程—煤化学工程]
  • 作者机构:[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, [2]中国科学院研究生院,北京100039
  • 相关基金:国家自然科学基金重大项目(20590361);国家高技术研究发展计划(863计划,2001AA523010):中国科学院知识创新重大项目(KGCSX1-SW-02).
  • 相关项目:F-T合成催化技术中的关键化学问题研究
中文摘要:

研究了Ni助剂对共沉淀型FeMnK/SiO2催化剂的结构性质和还原炭化行为的影响。结果表明,添加少量Ni助剂提高了催化剂的比表面积,降低了平均孔径,促进了催化剂中铁氧化物的分散。在H2-TPR中,Ni助剂降低了催化剂的还原温度;在CO-TPR中,Ni助剂使催化剂的还原和炭化峰前移,提高了氧的移除速率,增加了碳的引入量;在合成气等温还原中,Ni助剂提高了催化剂的活化速率,在相同的还原时间内可获得更高的F-T合成反应活性。

英文摘要:

Ni promoter was introduced into the co-precipitated FeMnK/SiO2 Fischer-Tropsch synthesis catalysts. The effects of Ni on catalyst structural properties, reduction and carburization behaviors were studied by N2 physical adsorption, XRD, Moessbauer spectroscopy, temperature programmed reduction (TPR) in H2 and CO, and isothermal reduction in syngas. The results indicate that Ni promoter increases the BET surface areas of catalysts and is favorable to the formation of smaller crystallite particles. H2-TPR results show that Ni decreases the reduction temperature of catalysts, and CO-TPR results show that Ni facilitates the oxygen removal and increases the carbon introduction content. These effects contribute to a significant improvement of the reduction and carburization behaviors of catalysts in syngas, and the promotion effect increases with the Ni loading content.

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