Abstract

This review mainly focuses on summarizing the different metal oxide systems utilized for water-splitting reaction using concentrated solar energy. Only two or three cyclic redox processes are considered. Particle size effect on redox reactions and economic aspect of hydrogen production via concentrated solar energy are also briefly discussed. Among various metal oxides system CeO2 system is emerging as a promising candidate and researchers have demonstrated workability of this system in the solar cavity-receiver reactor for over 500 cycles. The highest solar thermal process efficiency obtained so far is about 0.4 %, which needs to be increased for real commercial applications. Among traditionally studied oxides, thin-film ferrites looks more promising and could meet US Department of energy target of $2.42/kg H2 by 2025. The cost is mainly driven by high heliostat cost which needs to reduced significantly for economic feasibility. Overall, more work needs to be done in terms of redox material engineering, reactor technology, heliostat cost reduction and gas separation technologies before commercialization of this technology.

Highlights

  • Hydrogen is considered as generation fuel to propel airplanes, automotive vehicles and virtually any stationaryWater splitting by low valent metal oxides at high temperature is one of the clean way of hydrogen production since the temperature needed to perform chemical reaction comes from concentrated solar thermal heat

  • This review summarizes the work done in high-temperature hydrogen production via two-step redox processes

  • Several two- and three-step H2O-splitting thermochemical cycles based on metal oxides redox reactions have been reported in the literature

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Summary

Introduction

Water splitting by low valent metal oxides at high temperature is one of the clean way of hydrogen production since the temperature needed to perform chemical reaction comes from concentrated solar thermal heat. This review summarizes the work done in high-temperature hydrogen production via two-step redox processes

Results
Conclusion
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