2023
DOI: 10.1016/j.ijhydene.2022.11.035
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Techno-economic model and feasibility assessment of green hydrogen projects based on electrolysis supplied by photovoltaic PPAs

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Cited by 30 publications
(11 citation statements)
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“…Green hydrogen application can be an interesting alternative to be used as a storage method for the non-dispatchable renewable energy generated . In this regard, Spain has emerged as one of the leading European Countries in terms of projects promoting green hydrogen production . However, using hydrogen as an energy vector faces some challenges since hydrogen features a low volumetric energy density (4.5 MJ/L for compressed H 2 ) and a low boiling point (−253 °C) .…”
Section: Results and Discussionmentioning
confidence: 99%
See 1 more Smart Citation
“…Green hydrogen application can be an interesting alternative to be used as a storage method for the non-dispatchable renewable energy generated . In this regard, Spain has emerged as one of the leading European Countries in terms of projects promoting green hydrogen production . However, using hydrogen as an energy vector faces some challenges since hydrogen features a low volumetric energy density (4.5 MJ/L for compressed H 2 ) and a low boiling point (−253 °C) .…”
Section: Results and Discussionmentioning
confidence: 99%
“… 46 In this regard, Spain has emerged as one of the leading European Countries in terms of projects promoting green hydrogen production. 47 However, using hydrogen as an energy vector faces some challenges since hydrogen features a low volumetric energy density (4.5 MJ/L for compressed H 2 ) and a low boiling point (−253 °C). 5 For this reason, ammonia represents an interesting alternative hydrogen carrier to overcome the challenges associated with hydrogen transportation and storage because this compound features a higher volumetric energy density (12.9–14.4 MJ/L) and a higher boiling point (−33 °C) than hydrogen.…”
Section: Results and Discussionmentioning
confidence: 99%
“…6 shows the DC electrical consumption (red, left axis) and efficiency (% of HHV, green, right axis) vs output mass flow for the case of 1 MW electrolyzer. OPEX is assumed to be 3% of CAPEX /yr [7] (50.73 €/kW/year, which, supposing about 6,000 hours of operation per year, it will be about 0.008 €/kW/h of operation), and the cost of stack replacement 30% of CAPEX, being the lifetime for stack replacement 80,000 h of operation. Minimum partial load is 10% and hotstandby consumption 2% [7].…”
Section: Rectifier+ Electrolyzer + Compressor + Storage 4 X Wind Turb...mentioning
confidence: 99%
“…Regarding the water consumption, cost of water is assumed to be 3.8 €/m 3 and the consumption of water to produce hydrogen is 15 L/kg [7], therefore a cost of 0.057 €/kg of H2 produced will be considered for water consumption, which is almost negligible compared to the typical hydrogen selling prices of several € per kg.…”
Section: Rectifier+ Electrolyzer + Compressor + Storage 4 X Wind Turb...mentioning
confidence: 99%
“…Meeting the global energy demand while striving for net-zero goals presents a formidable challenge in today's world. Decarbonizing economic sectors and adopting non-pollutant energy sources are imperative steps toward achieving this objective (Acar & Dincer, 2022;Matute et al, 2022). Notably, a significant portion of CO2 emissions 86% emanates from power generation, transportation, and industrial activities (Ayodele et al, 2012;Jahangiri et al, 2020;Kojima et al, 2023).…”
Section: Introductionmentioning
confidence: 99%