Enhanced ethanol steam reforming by CO2 absorption using CaO, CaOMgO or Na2ZrO3

This paper presents results of thermodynamic analysis and experimental evaluation of hydrogen production by steam reforming of ethanol (SRE) combined with CO2 absorption using a mixture of a solid absorbent (CaO, CaO*MgO and Na2ZrO3) and a Ni/Al2O3 catalyst. Thermodynamic analysis results indicate t...

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Published inInternational journal of hydrogen energy Vol. 39; no. 29; pp. 16595 - 16607
Main Authors Aceves Olivas, D.Y., Baray Guerrero, M.R., Escobedo Bretado, M.A., Marques da Silva Paula, M., Salinas Gutiérrez, J., Guzmán Velderrain, V., López Ortiz, A., Collins-Martínez, V.
Format Journal Article Conference Proceeding
LanguageEnglish
Published Kidlington Elsevier Ltd 02.10.2014
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Abstract This paper presents results of thermodynamic analysis and experimental evaluation of hydrogen production by steam reforming of ethanol (SRE) combined with CO2 absorption using a mixture of a solid absorbent (CaO, CaO*MgO and Na2ZrO3) and a Ni/Al2O3 catalyst. Thermodynamic analysis results indicate that a maximum of 69.5% H2 (dry basis) is feasible at 1 atm, H2O/C2H5OH = 6 (molar ratio) and T = 600 °C. whereas, the addition of a CO2 absorbent at 1 atm, T = 600 °C and H2O/C2H5OH/Absorbent = 6:1:2.5, produced a H2 concentration of 96.6, 94.1, and 92.2% using CaO, CaO*MgO, and Na2ZrO3, respectively. SRE experimental evaluation achieved a maximum of 60% H2. While combining SRE and a CO2 absorbent exhibited a concentration of 96, 94, and 90% employing CaO, CaO*MgO, and Na2ZrO3, respectively at 1 atm, T = 600 °C, SV = 414 h−1 and H2O/C2H5OH/absorbent = 6:1:2.5 (molar ratio). [Display omitted] •Thermodynamic analysis & experimental H2 production by steam reforming of ethanol.•Enhanced steam reforming of ethanol using a solid CO2 absorbent.•Evaluation of Na2ZrO3 synthetic absorbent combined with ethanol steam reforming.
AbstractList This paper presents results of thermodynamic analysis and experimental evaluation of hydrogen production by steam reforming of ethanol (SRE) combined with CO2 absorption using a mixture of a solid absorbent (CaO, CaO*MgO and Na2ZrO3) and a Ni/Al2O3 catalyst. Thermodynamic analysis results indicate that a maximum of 69.5% H2 (dry basis) is feasible at 1 atm, H2O/C2H5OH = 6 (molar ratio) and T = 600 °C. whereas, the addition of a CO2 absorbent at 1 atm, T = 600 °C and H2O/C2H5OH/Absorbent = 6:1:2.5, produced a H2 concentration of 96.6, 94.1, and 92.2% using CaO, CaO*MgO, and Na2ZrO3, respectively. SRE experimental evaluation achieved a maximum of 60% H2. While combining SRE and a CO2 absorbent exhibited a concentration of 96, 94, and 90% employing CaO, CaO*MgO, and Na2ZrO3, respectively at 1 atm, T = 600 °C, SV = 414 h−1 and H2O/C2H5OH/absorbent = 6:1:2.5 (molar ratio). [Display omitted] •Thermodynamic analysis & experimental H2 production by steam reforming of ethanol.•Enhanced steam reforming of ethanol using a solid CO2 absorbent.•Evaluation of Na2ZrO3 synthetic absorbent combined with ethanol steam reforming.
Author Aceves Olivas, D.Y.
Escobedo Bretado, M.A.
Baray Guerrero, M.R.
Marques da Silva Paula, M.
Salinas Gutiérrez, J.
López Ortiz, A.
Guzmán Velderrain, V.
Collins-Martínez, V.
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Issue 29
Keywords H2 production
CO2 capture
Ethanol reforming
Na2ZrO3
Na
Ethanol
Hydrogen
production
ZrO
Carbon dioxide
CO2 sequestration
H
capture
Steam reforming
CO
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PublicationTitle International journal of hydrogen energy
PublicationYear 2014
Publisher Elsevier Ltd
Elsevier
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Snippet This paper presents results of thermodynamic analysis and experimental evaluation of hydrogen production by steam reforming of ethanol (SRE) combined with CO2...
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elsevier
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StartPage 16595
SubjectTerms Alternative fuels. Production and utilization
Applied sciences
CO2 capture
Energy
Ethanol reforming
Exact sciences and technology
Fuels
H2 production
Hydrogen
Na2ZrO3
Title Enhanced ethanol steam reforming by CO2 absorption using CaO, CaOMgO or Na2ZrO3
URI https://dx.doi.org/10.1016/j.ijhydene.2014.04.156
Volume 39
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