Hydrogen production by SI process, with electrodialysis stack embedded in HI decomposition
- Authors
- Kang, Kyoung-Soo; Kim, Chang-Hee; Kim, Jong-Won; Cho, Won-Chul; Jeong, Seong-Uk; Park, Chu-Sik; Park, Byung-Heung; Kang, Jeong-Won; Bae, Ki-Kwang
- Issue Date
- 2-Mar-2016
- Publisher
- PERGAMON-ELSEVIER SCIENCE LTD
- Keywords
- Sulfur-iodine process; Electrodialysis; Nuclear hydrogen; Thermochemical cycle; Water splitting
- Citation
- INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.41, no.8, pp 4560 - 4569
- Pages
- 10
- Indexed
- SCI
SCIE
SCOPUS
- Journal Title
- INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
- Volume
- 41
- Number
- 8
- Start Page
- 4560
- End Page
- 4569
- URI
- https://scholar.korea.ac.kr/handle/2021.sw.korea/89245
- DOI
- 10.1016/j.ijhydene.2015.12.101
- ISSN
- 0360-3199
1879-3487
- Abstract
- Hydrogen production by the sulfur-iodine (SI) process, with an electrodialysis (ED) stack embedded in the HI decomposition section (SEC3) to concentrate HI in the HIx solution and overcome the pseudo-azeotrope, was conducted under pressurized conditions. The HIx solution of H2O/HI = 5.63-6.13 and I-2/HI = 0.57-1.97 was supplied to the SEC3. HI gas was concentrated in a packed distillation column and decomposed over Pt/Al2O3. The experimental results of distillation column operation under different feed rates and HIx compositions are reported. The raffinate from the column showed a pseudo-azeotropic Hlx mixture, as predicted in previous research. The dynamic responses of the ED stack were examined during the start-up period according to the HIx feed composition at the anode inlet. The ED voltage changed with the I-2 concentration in the inlet flow. The proton transport number (t(+)) and electro-osmosis coefficient (beta) were estimated for the ED stack during the operations. Hydrogen production ranged from 18.3 to 50 L/h, depending on the operating conditions and HIx feed composition. Copyright (c) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
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