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Cost Analysis and Optimization of Green Hydrogen Production via Concentrating Solar Technologies and PEM Electrolyzer

集光型太陽熱技術とPEM電解によるグリーン水素製造のコスト分析と最適化 (AI 翻訳)

T. A. Tivfa, A. Shuaibu, Hussein A. Mohammed, A. Alquaity, O. Munteshari

International Journal of Energy Research📚 査読済 / ジャーナル2026-01-01#水素
DOI: 10.1155/er/3723245
原典: https://doi.org/10.1155/er/3723245

🤖 gxceed AI 要約

日本語

本研究では、太陽熱発電(SPTおよびPTC)とPEM電解槽を組み合わせたグリーン水素製造のコスト分析と最適化を実施。各種サイクル構成を比較し、LCOHは7.78~17.76$/kgと試算。容量係数が性能に最も影響し、多目的最適化により効率向上と低コスト化を達成。

English

This study analyzes and optimizes green hydrogen production costs using solar power towers (SPT) and parabolic trough collectors (PTC) with PEM electrolyzers. Levelized cost of hydrogen ranges from $7.78/kg to $17.76/kg. Capacity factor is the most influential parameter. Multi-objective optimization improves efficiency and reduces costs.

Unofficial AI-generated summary based on the public title and abstract. Not an official translation.

📝 gxceed 編集解説 — Why this matters

日本のGX文脈において

本論文は、日本の水素基本戦略で目標とする低コスト水素製造(2030年30円/Nm3)に関連する技術的知見を提供する。特に太陽熱利用の最適化は、再エネ賦存地域での水素製造コスト低減に示唆を与える。

In the global GX context

This paper provides technical insights for reducing green hydrogen costs, relevant to global hydrogen strategies including Japan's target of ¥30/Nm3 by 2030. The optimization of solar thermal technologies offers pathways for cost reduction in sun-rich regions.

👥 読者別の含意

🔬研究者:For researchers, this provides a comparative cost analysis and optimization framework for solar-driven hydrogen production.

🏢実務担当者:Practitioners can use the cost benchmarks and optimization methods for project feasibility studies.

🏛政策担当者:Policymakers can reference the cost ranges for hydrogen subsidy design and renewable hydrogen mandates.

📄 Abstract(原文)

The burgeoning demand for power across the globe and the disastrous effect of climate change that results from power generation through depleting unclean fuel sources have necessitated the use of renewable and clean fuels. Hydrogen is a good alternative but only when produced from low‐carbon energy resources. However, hydrogen production via this pathway has a high cost and low system efficiency. Therefore, a comparative cost analysis has been performed for hydrogen production through solar power tower (SPT) and parabolic trough collector (PTC) with proton exchange membrane (PEM) electrolyzer. This is carried out using different cycle configurations comprising a modified steam Rankine cycle (MSRC), supercritical carbon dioxide Brayton cycle (SCBC), and organic Rankine cycle (ORC). Optimization of the solar tower power configurations is also performed for improved system performance. The result of the analysis showed that all SPT’s configurations outperformed the PTC’s configurations except for the configuration comprising the steam Rankine cycle (SRC) and ORC due to how well it performed under the low operating temperature of the PTC system. The levelized cost of hydrogen (LCOH) ranged from 7.78 $/kg for the PTC‐MSRC‐ORC configuration to 17.76 $/kg for the PTC‐MSRC‐SCBC configuration. The parametric analysis of the system also showed that the capacity factor had the greatest influence on system performance. Furthermore, a multiobjective optimization of the system using a brute‐force algorithm for minimizing the LCOH and maximizing efficiency improved the system performance in all configurations.

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