Determination of Kinetic Parameters for Methane Oxidation over Pt/γ-Al2O3 in a Fixed-Bed Reactor

Authors

  • Vita Wonoputri Research Group of Chemical Engineering Process Design and Development, Faculty of Industrial Technology, Institut Teknologi Bandung
  • Mohammad Effendy Research Group of Chemical Engineering Process Design and Development, Faculty of Industrial Technology, Institut Teknologi Bandung
  • Yogi Wibisono Budhi Research Group of Chemical Engineering Process Design and Development, Faculty of Industrial Technology, Institut Teknologi Bandung
  • Yazid Bindar Research Group of Chemical Engineering Energy and Processing System, Faculty of Industrial Technology, Institut Teknologi Bandung
  • S. Subagjo Research Group of Chemical Engineering Process Design and Development, Faculty of Industrial Technology, Institut Teknologi Bandung

DOI:

https://doi.org/10.5614/j.eng.technol.sci.2013.45.2.7

Abstract

This paper describes akinetic study for the determination of the kinetic parameters of lean methane emission oxidation over Pt/γ-Al2O3 in a dedicated laboratory scale fixed bed reactor. A model ofthemechanistic reaction kinetic parameters has been developed. The reaction rate model was determined using therate-limiting step method, which was integrated and optimized to find the most suitable model and parameters. Based on this study, the Langmuir-Hinshelwood reaction rate model with the best correlationis the one where the rate-limiting step is thesurface reaction between methane and one adsorbed oxygen atom. The pre-exponential factor and activation energy were 9.19 x 105 and 92.04 kJ/mol, while the methane and oxygen adsorption entropy and enthalpy were "?17.46 J/mol.K, "?2739.36 J/mol,"?16.34 J/mol.K, and "?6157.09 J/mol, respectively.

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References

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Published

2013-07-01

How to Cite

Wonoputri, V., Effendy, M., Budhi, Y. W., Bindar, Y., & Subagjo, S. (2013). Determination of Kinetic Parameters for Methane Oxidation over Pt/γ-Al2O3 in a Fixed-Bed Reactor. Journal of Engineering and Technological Sciences, 45(2), 193-206. https://doi.org/10.5614/j.eng.technol.sci.2013.45.2.7

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