University of Limerick Institutional Repository

Computational simulation and modelling of uranium extraction using tributylphosphate through membrane extractor

DSpace Repository

Show simple item record

dc.contributor.advisor
dc.contributor.author Syah, Rahmad
dc.contributor.author Ramadan, Dadan
dc.contributor.author Elveny, Marischa
dc.contributor.author Cao, Yan
dc.contributor.author Khan, Afrasyab
dc.contributor.author Abdi, Hamid
dc.contributor.author Ghadiri, Mahdi
dc.date.accessioned 2021-09-13T11:13:06Z
dc.date.available 2021-09-13T11:13:06Z
dc.date.issued 2021
dc.identifier.uri http://hdl.handle.net/10344/10565
dc.description peer-reviewed en_US
dc.description.abstract Non-disperse solvent extraction is an effective technique for the extraction of metal ions from aqueous solution. In this study, uranium extraction using n-dodecane solvent containing tributylphosphate extractant in a membrane contactor was investigated. A 2D mathematical model was developed for the fluid flow and mass transfer in the hollow fibre membrane extractor. The equations of the created model were solved using the finite element method. The uranium concentration distribution in the extractor at different extractant concentrations as well as feed acidity was studied. The results showed that there is reasonable good agreement between experimental uranium extraction and modelling outputs at different extractant concentrations. Increasing extractant concentration from 5 to 30% led to the enhancement of uranium extraction from 2.60 to 34.13%. Also, there was an increase in the uranium extraction with increasing feed acidity in the range of 1–3 M. Furthermore, based on the radial uranium concentration distribution, it was found that the main mass transfer resistance in the system was microporous membrane section. Finally, it was obtained that the uranium extraction efficiency could be improved significantly by increasing porosity-to-tortuosity ratio. It was concluded that the membrane specification plays the most important role as the dominant mass transfer resistant was in the membrane subdomain en_US
dc.language.iso eng en_US
dc.publisher Nature en_US
dc.relation A03.21.0011 en_US
dc.relation.ispartofseries Scientifc Reports;11, 17818
dc.subject porosity-to-tortuosity ratio en_US
dc.subject membrane contactor en_US
dc.title Computational simulation and modelling of uranium extraction using tributylphosphate through membrane extractor en_US
dc.type info:eu-repo/semantics/article en_US
dc.type.supercollection all_ul_research en_US
dc.type.supercollection ul_published_reviewed en_US
dc.identifier.doi 10.1038/s41598-021-97379-0
dc.contributor.sponsor Government of the Russian Federation en_US
dc.rights.accessrights info:eu-repo/semantics/openAccess en_US


Files in this item

This item appears in the following Collection(s)

Show simple item record

Search ULIR


Browse

My Account

Statistics