Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent

Ethanol steam reforming with and without the presence of CaO as a CO 2 sorbent is modeled. Potential advantages of the presence of CaO as CO2 sorbent include higher energy efficiency, higher hydrogen production and lower CO content in the reformer gas exit. The presence of CaO eliminates the need of...

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Publicado: 2004
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Acceso en línea:https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_03787753_v138_n1-2_p61_Comas
http://hdl.handle.net/20.500.12110/paper_03787753_v138_n1-2_p61_Comas
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spelling paper:paper_03787753_v138_n1-2_p61_Comas2023-06-08T15:40:27Z Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent Ethanol reforming Fuel cell Hydrogen production Atmospheric pressure Carbon dioxide Computer simulation Energy efficiency Ethanol Fuel cells Lime Methane Thermodynamics Ethanol reforming Hydrogen production Thermal efficiency Thermodynamic analysis Hydrogen fuels Ethanol steam reforming with and without the presence of CaO as a CO 2 sorbent is modeled. Potential advantages of the presence of CaO as CO2 sorbent include higher energy efficiency, higher hydrogen production and lower CO content in the reformer gas exit. The presence of CaO eliminates the need of a WGS reactor for PEMFC application. Favorable operation conditions in the presence of CaO are (1) atmospheric pressure, (2) reactor temperatures around 700°C, and (3) water/ethanol molar ratio of 4. © 2004 Elsevier B.V. All rights reserved. 2004 https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_03787753_v138_n1-2_p61_Comas http://hdl.handle.net/20.500.12110/paper_03787753_v138_n1-2_p61_Comas
institution Universidad de Buenos Aires
institution_str I-28
repository_str R-134
collection Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA)
topic Ethanol reforming
Fuel cell
Hydrogen production
Atmospheric pressure
Carbon dioxide
Computer simulation
Energy efficiency
Ethanol
Fuel cells
Lime
Methane
Thermodynamics
Ethanol reforming
Hydrogen production
Thermal efficiency
Thermodynamic analysis
Hydrogen fuels
spellingShingle Ethanol reforming
Fuel cell
Hydrogen production
Atmospheric pressure
Carbon dioxide
Computer simulation
Energy efficiency
Ethanol
Fuel cells
Lime
Methane
Thermodynamics
Ethanol reforming
Hydrogen production
Thermal efficiency
Thermodynamic analysis
Hydrogen fuels
Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent
topic_facet Ethanol reforming
Fuel cell
Hydrogen production
Atmospheric pressure
Carbon dioxide
Computer simulation
Energy efficiency
Ethanol
Fuel cells
Lime
Methane
Thermodynamics
Ethanol reforming
Hydrogen production
Thermal efficiency
Thermodynamic analysis
Hydrogen fuels
description Ethanol steam reforming with and without the presence of CaO as a CO 2 sorbent is modeled. Potential advantages of the presence of CaO as CO2 sorbent include higher energy efficiency, higher hydrogen production and lower CO content in the reformer gas exit. The presence of CaO eliminates the need of a WGS reactor for PEMFC application. Favorable operation conditions in the presence of CaO are (1) atmospheric pressure, (2) reactor temperatures around 700°C, and (3) water/ethanol molar ratio of 4. © 2004 Elsevier B.V. All rights reserved.
title Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent
title_short Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent
title_full Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent
title_fullStr Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent
title_full_unstemmed Thermodynamic analysis of hydrogen production from ethanol using CaO as a CO2 sorbent
title_sort thermodynamic analysis of hydrogen production from ethanol using cao as a co2 sorbent
publishDate 2004
url https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_03787753_v138_n1-2_p61_Comas
http://hdl.handle.net/20.500.12110/paper_03787753_v138_n1-2_p61_Comas
_version_ 1768546495273893888