Solar hydrogen production: Technoeconomic analysis of a concentrated solar-powered high-temperature electrolysis system

被引:6
|
作者
Muhammad, Hafiz Ali [1 ]
Naseem, Mujahid [1 ]
Kim, Jonghwan [1 ]
Kim, Sundong [2 ]
Choi, Yoonseok [2 ]
Lee, Young Duk [1 ]
机构
[1] Korean Inst Energy Technol KENTECH, Dept Energy Engn, 21 KENTECH Gil, Naju 58330, South Korea
[2] Korea Inst Energy Res KIER, High Temp Energy Convers Lab, 152 Gajeong Ro, Daejeon 34129, South Korea
关键词
Green hydrogen; Solid -oxide electrolysis -cell; Concentrated solar power; Economics; SOLID OXIDE ELECTROLYZER; THERMAL-ENERGY STORAGE; PERFORMANCE ANALYSIS; RENEWABLE ENERGY; HYBRID SYSTEM; OPTIMIZATION; PLANTS; COST;
D O I
10.1016/j.energy.2024.131284
中图分类号
O414.1 [热力学];
学科分类号
摘要
Hydrogen is considered a key energy vector and carrier for the decarbonization of global energy systems. However, the economics of green hydrogen systems hinder their widespread application. This paper presents a techno-economic analysis of a green hydrogen production system using high-temperature water electrolysis integrated with a concentrated solar power system (CSP-SOEC) for Western Australia. Real-time solar resource data with 30-min resolution for a typical meteorological year were used to assess the performance of the entire system. The intermittent nature of solar resources is accounted for by integrating the system with a thermal energy storage medium and performing the analysis in off-design mode. The validity of the electrolysis stack model is crucial for overall system performance, which was confirmed through experimental testing conducted on a 15-cell stack. The system was designed to generate a 1 MWe output, and the results showed that a field area of 29,000 m2 and thermal energy storage capacity of 382,500 kWh can fulfil the design criteria. The system generates 0.86 tonne/day of hydrogen at a cost of 8.87 US$/kg-H2 with a solar-to-hydrogen efficiency of 13.80 %. The cost breakdown revealed that the storage medium has the most significant contribution. Moreover, the sensitivity of the system to the production capacity was analyzed, which showed that larger-scale hydrogen production systems have the potential to further reduce the cost. An 8 MWe system has the capacity to produce 7.18 tonne/day of hydrogen at a cost of 6.1 US$/kg-H2. The molten salt is currently utilized only 39.3 % for the hydrogen production process. To optimize resource utilization, a cogeneration system is devised and assessed for simultaneous steam and hydrogen production. The results reveal that the cogeneration system can achieve an LCOH reduction of 9 % by reaching 8.07 US$/kg-H2. These findings are invaluable for academic and industry stakeholders in making informed decisions and fostering the green hydrogen sector in Australia.
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页数:17
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