Y. WanSouth-Central University for Nationalities Key Laboratory of Catalysis and Materials Science of Hubei Province, College of Chemistry and Materials Science Wuhan 430074 China
J. LiSouth-Central University for Nationalities Key Laboratory of Catalysis and Materials Science of Hubei Province, College of Chemistry and Materials Science Wuhan 430074 China
D. ChenSouth-Central University for Nationalities Key Laboratory of Catalysis and Materials Science of Hubei Province, College of Chemistry and Materials Science Wuhan 430074 China
The reduction process of silica supported cobalt catalyst was studied by thermal analysis technique. The reduction of the
catalyst proceeds in two steps:
which was validated by the TPR and in-situ XRD experiments. The kinetic parameters of the reduction process were obtained with a comparative method. For the first step,
the activation energy, Ea, and the pre-exponential factor, A, were found to be 104.35 kJ mol−1 and 1.18�106∼2.45�109 s−1 respectively. The kinetic model was random nucleation and growth and the most probable mechanism function was found to be
f(α)=3/2(1−α)[−ln(1−α)]1/3 or in the integral form: g(α)=[−ln(1−α)]2/3. For the second step, the activation energy, Ea, and the pre-exponential factor, A, were found to be 118.20 kJ mol−1 and 1.75�107∼2.45 � 109s−1 respectively. The kinetic model was a second order reaction and the probable mechanism function was f(α)=(1−α)2 or in the integral form: g(α)=[1−α]−1−1.