Oguzhan Kivan , Muhammad Yusuf , Rachael Filson-Halliwell , Jennifer N. Enemmoh , David Harbottle , Timothy N. Hunter
{"title":"Intensified co-precipitation and ion exchange using an agitated tubular reactor (ATR) for enhanced removal of Cs+ and Sr2+ ions","authors":"Oguzhan Kivan , Muhammad Yusuf , Rachael Filson-Halliwell , Jennifer N. Enemmoh , David Harbottle , Timothy N. Hunter","doi":"10.1016/j.cep.2024.110077","DOIUrl":null,"url":null,"abstract":"<div><div>Composite coagulants were synthesised in both a batch system and an agitated tubular reactor (ATR) using natural clinoptilolite with barite (BaSO<sub>4</sub>) co-precipitation for the intensified simultaneous removal of Cs<sup>+</sup> and Sr<sup>2+</sup> ions. Ideal plug-flow characterisation of ATR was initially assessed under 3 and 5 Hz oscillations, showing pseudo plug-flow behaviour at the higher rate. Composite flocs were characterised by SEM and size analysis, while dewaterability was also studied by sedimentation and pressure filtration. Aggregate sizes were smaller, but denser and more monodisperse from the ATR than in batch. Composite flocs also gave measured specific cake resistances > 10 × smaller than pure BaSO<sub>4</sub>. The higher metal removal performance was achieved using the ATR for Cs<sup>+</sup> (95.7%) and Sr<sup>2+</sup> (99.9%) at 5 Hz oscillation. A further enhancement for Cs<sup>+</sup> removal was achieved by introducing Ba<sup>2+</sup> ions into ATR after Na<sub>2</sub>SO<sub>4</sub> addition, achieving > 96% Cs<sup>+</sup> and > 99.9% Sr<sup>2+</sup> removal. Overall, this study highlights that composite flocs outperform pure BaSO<sub>4</sub> in Cs<sup>+</sup> and Sr<sup>2+</sup> ion removal while achieving greater dewaterability and filterability. Additionally, we show the ATR effectively intensified the co-precipitation process, potentially reducing plant size and cost, making it a suitable process for modular nuclear cleanup and post-management operations.</div></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"207 ","pages":"Article 110077"},"PeriodicalIF":3.8000,"publicationDate":"2024-11-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering and Processing - Process Intensification","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S025527012400415X","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
Abstract
Composite coagulants were synthesised in both a batch system and an agitated tubular reactor (ATR) using natural clinoptilolite with barite (BaSO4) co-precipitation for the intensified simultaneous removal of Cs+ and Sr2+ ions. Ideal plug-flow characterisation of ATR was initially assessed under 3 and 5 Hz oscillations, showing pseudo plug-flow behaviour at the higher rate. Composite flocs were characterised by SEM and size analysis, while dewaterability was also studied by sedimentation and pressure filtration. Aggregate sizes were smaller, but denser and more monodisperse from the ATR than in batch. Composite flocs also gave measured specific cake resistances > 10 × smaller than pure BaSO4. The higher metal removal performance was achieved using the ATR for Cs+ (95.7%) and Sr2+ (99.9%) at 5 Hz oscillation. A further enhancement for Cs+ removal was achieved by introducing Ba2+ ions into ATR after Na2SO4 addition, achieving > 96% Cs+ and > 99.9% Sr2+ removal. Overall, this study highlights that composite flocs outperform pure BaSO4 in Cs+ and Sr2+ ion removal while achieving greater dewaterability and filterability. Additionally, we show the ATR effectively intensified the co-precipitation process, potentially reducing plant size and cost, making it a suitable process for modular nuclear cleanup and post-management operations.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.