Publication: Thermodynamic analysis and experimental study of hydrogen production from oxidative reforming of n-butanol
Issued Date
2015-06-20
Resource Type
ISSN
13858947
Other identifier(s)
2-s2.0-84946482448
Rights
Mahidol University
Rights Holder(s)
SCOPUS
Bibliographic Citation
Chemical Engineering Journal. Vol.278, (2015), 2-12
Suggested Citation
Unalome Wetwatana Hartley, Suksun Amornraksa, Pattaraporn Kim-Lohsoontorn, Navadol Laosiripojana Thermodynamic analysis and experimental study of hydrogen production from oxidative reforming of n-butanol. Chemical Engineering Journal. Vol.278, (2015), 2-12. doi:10.1016/j.cej.2015.02.016 Retrieved from: https://repository.li.mahidol.ac.th/handle/20.500.14594/35701
Research Projects
Organizational Units
Authors
Journal Issue
Thesis
Title
Thermodynamic analysis and experimental study of hydrogen production from oxidative reforming of n-butanol
Abstract
© 2015 Elsevier B.V. A Gibbs free energy minimization method was applied to analyze the thermodynamics of hydrogen production via oxidative reforming of n-butanol. The conditions studied were a temperature range of 300-1100 °C under atmospheric pressure with steam to n-butanol molar feed ratios (SBR) ranging from 0 to 12 and oxygen to n-butanol molar feed ratios (OBR) of 0-6. The thermoneutral conditions can be obtained at OBR of 2.70-2.80 at 700 °C and 2.65-2.75 at 800 °C, respectively. The maximum hydrogen yield of 5.56 mol/molButanol can be achieved at 700 °C with SBR of 12, conditions under which carbon formation and methane generation are predicted to be relatively low. The thermodynamic predictions were in good agreement with experimental results using Ni/Al2O3 and Rh/Al2O3 catalysts, from which the reaction was studied at different SBR, OBR, and temperatures. Under atmospheric pressure at 700 °C with OBR of 2.70 and SBR of 9, the product yields from the reaction in the presence of Rh/Al2O3 were close to the thermodynamic values.
