Design of integrated laboratory‐scale iodine sulfur hydrogen production cycle at INET. (14th April 2016)

• Record Type: Journal Article
• Authors: Zhang, Ping; Zhou, Chenglin; Guo, Hanfei; Chen, Songzhe; Wang, Laijun; Xu, Jingming
• Is Part Of: International journal of energy research. Volume 40:Number 11(2016)
• Page Start: 1509
• Page End: 1517
• Publication Date: 2016-04-14
• Subjects: iodine sulfur process -- integrated laboratory‐scale facility -- mass balance -- flowsheet design -- nuclear hydrogen production; Power resources -- Periodicals; Power (Mechanics) -- Periodicals; Power resources -- Research -- Periodicals; 621.042
• DOI: 10.1002/er.3535
• Languages: English
• ISSNs: 0363-907X

Abstract

Summary: The iodine sulfur (IS) thermochemical water‐splitting process, which has various merits, is considered as one of the most promising nuclear hydrogen production methods and has been intensively studied by many institutions. At the Institute of Nuclear and New Energy Technology of Tsinghua University in China, a proof‐of‐concept closed IS facility was built, and a closed‐cycle experiment was conducted. Currently, as a prospective research item of the high‐temperature gas‐cooled reactor demonstration plant project, an integrated laboratory‐scale IS facility (IS‐100) that aims to achieve long‐term stable operation of IS cycle is being developed, and the design and optimization of the flowsheet for the IS cycle are conducted. The specifications of the facility are presented along with simulation models. Mass balance and compositions of the streams in the Bunsen, sulfuric acid, and HI sections are calculated using Aspen Plus software with OLI database and embedded self‐made models. Based on the comparison between mass of recycled streams and heat requirements as well as sensitivity analysis, the optimized flowsheet and the operational parameters are proposed. In addition, the preliminary closed cycle experiment results on IS‐100 were presented, and the efficiency of the IS process and the R&D efforts to improve its efficiency are discussed. Copyright © 2016 John Wiley & Sons, Ltd. Abstract : An integrated laboratory‐scale IS facility with H2 production rate of 100NL/h was designed and built. The specifications of the facility are presented. Mass balance and compositions of the streams in the process are calculated using Aspen Plus software with OLI database, and embedded self‐made models, the optimized flow sheet and the operational parameters are proposed. The preliminary closed cycle experiment results on IS‐100 were presented.