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Hydrogen Production by Thermochemical Water Splitting; Membrane IS Process

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CO2 Free Ammonia as an Energy Carrier
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Abstract

The concept of the membrane iodine–sulfur (IS) process to produce H2 by the thermochemical decomposition of water with solar heat of approximately 650 °C was proposed. In the conventional IS process, the decomposition of SO3 in the H2SO4 decomposition process requires a high temperature heat of approximately 900 °C. As SO3 will be decomposed at 650 °C when using solar heat, a technology to improve the conversion rate in the SO3 decomposition reaction is required. In addition, the conventional IS process has technical problems such as excessive amount of I2 required in the Bunsen reaction (approx. nine times the amount required for the reaction) and a low conversion rate in the HI decomposition reaction. To solve these problems, research was conducted to apply membrane technology to the three main reactions of the IS process, namely the Bunsen reaction, SO3 decomposition, and HI decomposition. The thermal mass balance calculation of the membrane IS process showed that the H2 production efficiency of 40% or more can be obtained at 650 °C.

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Correspondence to Shinji Kubo .

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Kubo, S., Sakaba, N., Inagaki, Y., Hosono, Y. (2023). Hydrogen Production by Thermochemical Water Splitting; Membrane IS Process. In: Aika, Ki., Kobayashi, H. (eds) CO2 Free Ammonia as an Energy Carrier. Springer, Singapore. https://doi.org/10.1007/978-981-19-4767-4_11

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