2015
DOI: 10.1016/j.enconman.2015.03.031
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Life cycle assessment of hydrogen and power production by supercritical water reforming of glycerol

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Cited by 44 publications
(11 citation statements)
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“…emissions from SS3 should not be considered as fossil carbon, but as biogenic CO2. This decision agrees with a study on the production of hydrogen and electricity by reforming supercritical water from bioglycerol feedstock (Galera and Gutiérrez-Ortiz, 2015). If CO2…”
Section: Life Cycle Profile Of the Processsupporting
confidence: 91%
“…emissions from SS3 should not be considered as fossil carbon, but as biogenic CO2. This decision agrees with a study on the production of hydrogen and electricity by reforming supercritical water from bioglycerol feedstock (Galera and Gutiérrez-Ortiz, 2015). If CO2…”
Section: Life Cycle Profile Of the Processsupporting
confidence: 91%
“…Nevertheless, the capital investment and operational difficulties of ASCWR process leads to relatively high hydrogen production costs (5.75 $/kg). This value is still too high compared to conventional technologies (e.g., methane SR); in a future scenario, however, some possible improvements in supercritical water (SCW) reforming performance may lead to a decrease in the estimated renewable hydrogen price [130,131].…”
Section: Life Cycle Assessment (Lca) Approach For a Sustainable Hydromentioning
confidence: 99%
“…The GWP values fell in the interval between 0.28 and 0.52 kg CO 2 eq./kWh for the APG system and between 0.12 kg and 0.96 kg CO 2 eq./kWh for the COG case. These results were in the range of values that characterize the carbon footprint of natural gas-fired power generation [66,67]. The contribution of the hydrogen recovery stage in this category is much greater than that of the cell, being between 82% and 90% for the APG case and from 61% to 95% for the COG system.…”
Section: Life-cycle Impact Assessment Based On Energy Productionmentioning
confidence: 67%