O. Balteanu, A. Bornea, I. Ștefan, I. Făurescu, G. Ana, C. Bucur, M. Zamfirache
{"title":"The influence of non-steady state operation of a PEM electrolyzer on hydrogen isotope separation in a CECE process","authors":"O. Balteanu, A. Bornea, I. Ștefan, I. Făurescu, G. Ana, C. Bucur, M. Zamfirache","doi":"10.1016/j.fusengdes.2025.115127","DOIUrl":null,"url":null,"abstract":"<div><div>The electrolyzer is one of the main components of the Combined Electrolysis and Catalytic Exchange (CECE) process used to provide isotopic enrichment of hydrogen. The CECE process demands that the electrolyzer run under constant operating parameters (mainly the flowrate and water hold-up). The influence of the non-steady state regime for an electrolyzer equipped with a proton exchange membrane (PEM) stack cell, has been investigated, considering variations of the water hold-up, induced by the water management in the cathode and anode circuits. Based on a mathematical model written for a constant hold-up, a new mathematical model was developed to simulate the tritium enrichment, considering different variation of the hold-up between two limits determined from experimental data. Tests with tritiated water were carried out to evaluate the influence of the electrolyzer’s water hold-up variation on the isotopic separation process and to verify the mathematical model.</div></div>","PeriodicalId":55133,"journal":{"name":"Fusion Engineering and Design","volume":"216 ","pages":"Article 115127"},"PeriodicalIF":1.9000,"publicationDate":"2025-04-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Fusion Engineering and Design","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0920379625003242","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"NUCLEAR SCIENCE & TECHNOLOGY","Score":null,"Total":0}
引用次数: 0
Abstract
The electrolyzer is one of the main components of the Combined Electrolysis and Catalytic Exchange (CECE) process used to provide isotopic enrichment of hydrogen. The CECE process demands that the electrolyzer run under constant operating parameters (mainly the flowrate and water hold-up). The influence of the non-steady state regime for an electrolyzer equipped with a proton exchange membrane (PEM) stack cell, has been investigated, considering variations of the water hold-up, induced by the water management in the cathode and anode circuits. Based on a mathematical model written for a constant hold-up, a new mathematical model was developed to simulate the tritium enrichment, considering different variation of the hold-up between two limits determined from experimental data. Tests with tritiated water were carried out to evaluate the influence of the electrolyzer’s water hold-up variation on the isotopic separation process and to verify the mathematical model.
期刊介绍:
The journal accepts papers about experiments (both plasma and technology), theory, models, methods, and designs in areas relating to technology, engineering, and applied science aspects of magnetic and inertial fusion energy. Specific areas of interest include: MFE and IFE design studies for experiments and reactors; fusion nuclear technologies and materials, including blankets and shields; analysis of reactor plasmas; plasma heating, fuelling, and vacuum systems; drivers, targets, and special technologies for IFE, controls and diagnostics; fuel cycle analysis and tritium reprocessing and handling; operations and remote maintenance of reactors; safety, decommissioning, and waste management; economic and environmental analysis of components and systems.