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水分压对铁基费托合成催化剂还原动力学的影响
引用本文:王洪,杨勇,吴宝山,许健,王虎林,青明,相宏伟,李永旺.水分压对铁基费托合成催化剂还原动力学的影响[J].催化学报,2010,31(2):205-212.
作者姓名:王洪  杨勇  吴宝山  许健  王虎林  青明  相宏伟  李永旺
作者单位: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;中国科学院研究生院,北京,100049
2. 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
基金项目:国家杰出青年科学基金(20625620);;国家自然科学基金(20703054)
摘    要: 利用恒温还原和程序升温还原技术研究了水分压对铁基费托合成催化剂还原路径、还原机理和表观活化能的影响. 程序升温还原结果表明, 水分压对催化剂的还原路径没有明显的影响, 催化剂均首先由 α-Fe2O3 还原为 Fe3O4, 然后超顺磁态 Fe3O4 先还原为 FeO, 再还原为 α-Fe, 而顺磁态 Fe3O4 则直接还原为 α-Fe. 恒温还原结果表明, 催化剂在 2.5%H2O-97.5%H2 气氛中还原时, 还原过程达到平衡时的还原程度随还原温度的升高而增加. 利用 Hancock-Sharp 方法分析了恒温还原过程的动力学模型. 结果表明, 还原温度较低时, 催化剂在 2.5%H2O-97.5%H2 气氛中还原时受内扩散模型控制; 还原温度较高时则受晶相形成与生长模型控制. 利用 Kissinger 方法计算了还原过程的活化能, 发现随着水分压的增加, 表观活化能呈增大的趋势. 水分压对 Fe3O4 还原为 α-Fe 过程的影响大于其对 α-Fe2O3 还原为 Fe3O4 过程的影响.

关 键 词:水分压  费托合成  铁基催化剂  还原动力学  表观活化能
收稿时间:2010-02-25

Effect of H2O Partial Pressure on Reduction Kinetics of Iron-Based Fischer-Tropsch Catalyst
WANG Hong,YANG Yong,WU Baoshan,XU Jian,WANG Hulin,QING Ming,XIANG Hongwei,LI Yongwang.Effect of H2O Partial Pressure on Reduction Kinetics of Iron-Based Fischer-Tropsch Catalyst[J].Chinese Journal of Catalysis,2010,31(2):205-212.
Authors:WANG Hong  YANG Yong  WU Baoshan  XU Jian  WANG Hulin  QING Ming  XIANG Hongwei  LI Yongwang
Institution:1State Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, Shanxi, China 2Graduate University of Chinese Academy of Sciences, Beijing 100049, China
Abstract:The effect of H_2O partial pressure on the reduction pathway, mechanism, and apparent activation energy of an iron-based Fischer-Tropsch catalyst was investigated by isothermal and temperature-programmed reduction (TPR). The TPR results indicated that the H_2O partial pressure had no obvious influence on the reduction pathway of the catalyst in H_2. α-Fe_2O_3 in the catalyst was first reduced to Fe_3O_4. The formed superparamagnetie Fe_3O_4 was reduced to a-Fe via FeO as an intermediate, while the formed paramagnetic Fe_3O_4 was reduced to α-Fe directly. The isothermal reduction of the catalyst showed that the reduction degree of the catalyst increased with the increase of reduction temperature when the reaction approached to equilibrium. The reduction mechanism analyzed based on the Hancock-Sharp method indicated that the reduction of the catalyst in 2.5%H_2O-97.5%H_2 at lower temperature was controlled by the inner diffusion model. However, at higher temperature the reduction process was controlled by the formation and growth of nuclei model. The apparent activation energy calculated based on the Kissinger method was increased with increasing H_2O partial pressure in H_2. The H_2O partial pressure had stronger influence on the reduction of Fe_3O_4 to α-Fe than that on the reduction of α-Fe_2O_3 to Fe_3O_4.
Keywords:water partial pressure  Fischer-Tropsch synthesis  iron-based catalyst  reduction kinetics  apparent activation energy  
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