TY - JOUR
T1 - Wind-powered hydrogen refueling station with energy recovery for green mobility in sustainable cities
AU - Sezer, Nurettin
AU - Bayhan, Sertac
N1 - Publisher Copyright:
© 2025 The Authors
PY - 2025/1/27
Y1 - 2025/1/27
N2 - This study presents the conceptual design and evaluation of an HRS for light-duty FCEVs. The proposed system integrates wind turbines, a water electrolyzer, three-stage hydrogen compressor, heat recovery and storage, a two-stage Organic Rankine Cycle (TS-ORC), hydrogen storage tanks, a Vapor Compression Refrigeration Cycle (VCRC), and a hydrogen dispenser. Waste heat from the hydrogen compression process is harnessed to power the TS-ORC, where the first stage drives the VCRC and the second stage generates additional electricity. A comprehensive assessment of the system confirmed the system's compliance with the principles of thermodynamics. The results indicate an overall system efficiency of 25.4 %, and the wind turbines alone achieve 46.21 % efficiency. The overall exergy destruction rate of the system is computed to be 2,120 kW and the main exergy destruction occurs in wind turbines and water electrolyzer. The first and second stages of the ORC exhibit efficiencies of 14.45 % and 6.05 %, respectively, while the VCRC yields a Coefficient of Performance (COP) of 1.24. The specific energy consumption for electrolytic hydrogen production, compression, and pre-cooling are calculated as 58.83, 1.99, and 0.29 kWh/kg, respectively. The hydrogen dispenser fills an onboard hydrogen storage tank with a 4 kg capacity at 700 bar in 5.5 min.
AB - This study presents the conceptual design and evaluation of an HRS for light-duty FCEVs. The proposed system integrates wind turbines, a water electrolyzer, three-stage hydrogen compressor, heat recovery and storage, a two-stage Organic Rankine Cycle (TS-ORC), hydrogen storage tanks, a Vapor Compression Refrigeration Cycle (VCRC), and a hydrogen dispenser. Waste heat from the hydrogen compression process is harnessed to power the TS-ORC, where the first stage drives the VCRC and the second stage generates additional electricity. A comprehensive assessment of the system confirmed the system's compliance with the principles of thermodynamics. The results indicate an overall system efficiency of 25.4 %, and the wind turbines alone achieve 46.21 % efficiency. The overall exergy destruction rate of the system is computed to be 2,120 kW and the main exergy destruction occurs in wind turbines and water electrolyzer. The first and second stages of the ORC exhibit efficiencies of 14.45 % and 6.05 %, respectively, while the VCRC yields a Coefficient of Performance (COP) of 1.24. The specific energy consumption for electrolytic hydrogen production, compression, and pre-cooling are calculated as 58.83, 1.99, and 0.29 kWh/kg, respectively. The hydrogen dispenser fills an onboard hydrogen storage tank with a 4 kg capacity at 700 bar in 5.5 min.
KW - Electrolysis
KW - Energy storage
KW - Fuel cell electric vehicle
KW - Heat recovery
KW - Hydrogen
KW - Hydrogen refueling station
UR - https://www.scopus.com/pages/publications/85216537276
U2 - 10.1016/j.ecmx.2025.100900
DO - 10.1016/j.ecmx.2025.100900
M3 - Article
AN - SCOPUS:85216537276
SN - 2590-1745
VL - 26
JO - Energy Conversion and Management: X
JF - Energy Conversion and Management: X
M1 - 100900
ER -