{"title":"Development of a prototype of helium-heated sulfuric acid decomposer for sulfur-family thermochemical water splitting process","authors":"Songzhe Chen , Peng Zhang , Laijun Wang , Peng Xiao , Wei Peng , Ping Zhang","doi":"10.1016/j.ijhydene.2025.151782","DOIUrl":null,"url":null,"abstract":"<div><div>The thermochemical iodine-sulfur (IS) and hybrid sulfur (HyS) cycles are among the most promising methods for large-scale hydrogen production, utilizing heat from high-temperature gas-cooled reactors (HTGRs) to achieve high efficiency and zero carbon dioxide emissions. The decomposition of sulfuric acid is a pivotal reaction in both IS and HyS technologies, occurring at the highest temperature and requiring the most heat input. The sulfuric acid decomposer (SAD) is a critical component that utilizes nuclear heat to facilitate sulfuric acid decomposition while simultaneously functioning as a process heat exchanger. In this study, the material balance of SAD as well as the flow rate and temperature distribution in the reactor were estimated through simulation, and a shell-and-tube SAD prototype was designed and manufactured based on the simulation data. A high-temperature helium heating circuit was established to investigate the thermohydraulic properties of the SAD prototype. Temperature distribution data for the interior and critical areas of the prototype were obtained when using helium as the heat source. The research results indicated that the heat exchanger efficiency of the decomposer can reach approximately 60 %. The sulfuric acid decomposition process was successfully validated at reaction temperature of higher than 800 °C. An oxygen production rate of 1.1 Nm<sup>3</sup>/h (corresponding to a hydrogen production rate of 2.2 Nm<sup>3</sup>/h of IS and HyS cycles) was achieved, and the decomposition reaction efficiency is about 70 %. These results confirmed the prototype's integrity, sealing performance, heat transfer efficiency, and chemical reaction capabilities under real conditions. The SAD prototype developed in this study represents the first reported instance of a decomposer constructed from engineering materials and heated by helium, and provides a significant reference for IS and HyS cycle water splitting technologies that utilize heat from HTGRs.</div></div>","PeriodicalId":337,"journal":{"name":"International Journal of Hydrogen Energy","volume":"180 ","pages":"Article 151782"},"PeriodicalIF":8.3000,"publicationDate":"2025-09-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Hydrogen Energy","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0360319925047858","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
引用次数: 0
Abstract
The thermochemical iodine-sulfur (IS) and hybrid sulfur (HyS) cycles are among the most promising methods for large-scale hydrogen production, utilizing heat from high-temperature gas-cooled reactors (HTGRs) to achieve high efficiency and zero carbon dioxide emissions. The decomposition of sulfuric acid is a pivotal reaction in both IS and HyS technologies, occurring at the highest temperature and requiring the most heat input. The sulfuric acid decomposer (SAD) is a critical component that utilizes nuclear heat to facilitate sulfuric acid decomposition while simultaneously functioning as a process heat exchanger. In this study, the material balance of SAD as well as the flow rate and temperature distribution in the reactor were estimated through simulation, and a shell-and-tube SAD prototype was designed and manufactured based on the simulation data. A high-temperature helium heating circuit was established to investigate the thermohydraulic properties of the SAD prototype. Temperature distribution data for the interior and critical areas of the prototype were obtained when using helium as the heat source. The research results indicated that the heat exchanger efficiency of the decomposer can reach approximately 60 %. The sulfuric acid decomposition process was successfully validated at reaction temperature of higher than 800 °C. An oxygen production rate of 1.1 Nm3/h (corresponding to a hydrogen production rate of 2.2 Nm3/h of IS and HyS cycles) was achieved, and the decomposition reaction efficiency is about 70 %. These results confirmed the prototype's integrity, sealing performance, heat transfer efficiency, and chemical reaction capabilities under real conditions. The SAD prototype developed in this study represents the first reported instance of a decomposer constructed from engineering materials and heated by helium, and provides a significant reference for IS and HyS cycle water splitting technologies that utilize heat from HTGRs.
期刊介绍:
The objective of the International Journal of Hydrogen Energy is to facilitate the exchange of new ideas, technological advancements, and research findings in the field of Hydrogen Energy among scientists and engineers worldwide. This journal showcases original research, both analytical and experimental, covering various aspects of Hydrogen Energy. These include production, storage, transmission, utilization, enabling technologies, environmental impact, economic considerations, and global perspectives on hydrogen and its carriers such as NH3, CH4, alcohols, etc.
The utilization aspect encompasses various methods such as thermochemical (combustion), photochemical, electrochemical (fuel cells), and nuclear conversion of hydrogen, hydrogen isotopes, and hydrogen carriers into thermal, mechanical, and electrical energies. The applications of these energies can be found in transportation (including aerospace), industrial, commercial, and residential sectors.