Приказ основних података о документу

dc.creatorČomor, Jožef J.
dc.creatorTolic, AS
dc.creatorKopečni, Miroslav M.
dc.creatorPetković, Đorđe M.
dc.date.accessioned2018-03-01T18:40:36Z
dc.date.available2018-03-01T18:40:36Z
dc.date.issued1999
dc.identifier.issn0149-6395
dc.identifier.urihttps://vinar.vin.bg.ac.rs/handle/123456789/2227
dc.description.abstractA mathematical model developed for the equilibrium HNO3-UO2(NO3)(2)-tri-n-butyl phosphate (TBP)-diluent is the basis of the computation of distribution isotherms. The isotherms are used to study the influence of TBP concentration on two chosen operation parameters, distribution coefficients and number of theoretical stages, for the selected flow sheets. It is established that an increase in TBP concentration leads to a decrease in the number of theoretical stages for the extraction flow sheets but to their increase for the stripping flow sheets. Given diagrams can be used to determine the efficiency of extraction processes. Agreement with available literature calculations on the number of theoretical stages supports the use of our model in the computation of distribution isotherms, of the system quoted above, in a wide range of nitric acid, uranyl nitrate, and TBP concentrations.en
dc.rightsrestrictedAccessen
dc.sourceSeparation Science and Technologyen
dc.titleModeling of the simultaneous extraction of nitric acid and uranyl nitrate with tri-n-butyl phosphate. Application to extraction operationen
dc.typearticleen
dcterms.abstractЦомор, ЈЈ; Копецни, ММ; Петковиц, ДМ; Толиц, AС;
dc.citation.volume34
dc.citation.issue1
dc.citation.spage115
dc.citation.epage122
dc.identifier.wos000078523800009
dc.identifier.doi10.1081/SS-100100640
dc.citation.rankM21
dc.identifier.scopus2-s2.0-0344849459


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