Abstract
A kinetic study of ethanol steam reforming to produce hydrogen within the region of kinetic rate control was carried out. A Ni(II)–Al(III) lamellar double hydroxide as catalyst precursor was used. H2, CO, CO2 and CH4 were obtained as products. Using the Langmuir–Hinshelwood (L–H) approach, two kinetic models were proposed. The first was a general model including four reactions, two of them corresponding to ethanol steam reforming and the other two to methane steam reforming. When high temperatures and/or high water/ethanol feed ratios were used, the system could be reduced to two irreversible ethanol steam reforming reactions.
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Abbreviations
- Ct :
-
Total concentration of active sites
- Ea :
-
Activation energy (KJ/mol)
- K:
-
Equilibrium constant
- K*:
-
Equilibrium constant of surface reaction
- KE :
-
Adsorption equilibrium constant of ethanol
- KM :
-
Adsorption equilibrium constant of methane
- KW :
-
Adsorption equilibrium constant of water
- k:
-
Kinetic coefficient
- k*:
-
k/Ct
- n :
-
Number of experiments
- P:
-
Partial pressure
- r:
-
Reaction rate
- y:
-
Molar fraction
- \( y_{i,s}^{\exp } \) :
-
Molar fraction of i measured in experiment s
- \( \hat{y}_{i}^{\exp } \) :
-
Average of y i,s exp
- y i,s :
-
Molar fraction of i predicted with the model
- ΔH:
-
Adsorption enthalpy
- \( \theta \) :
-
Space time
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Acknowledgments
To Universidad de Buenos Aires, CONICET, ANPCYT and CYTED for the financial support. The authors acknowledge the help of Mr. Roberto Tejeda in the experimental measurements.
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Mas, V., Bergamini, M.L., Baronetti, G. et al. A Kinetic Study of Ethanol Steam Reforming Using a Nickel Based Catalyst. Top Catal 51, 39–48 (2008). https://doi.org/10.1007/s11244-008-9123-y
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DOI: https://doi.org/10.1007/s11244-008-9123-y