Mostrar el registro sencillo del ítem

dc.contributor.authorDascalu, Mihaela-Elena
dc.contributor.authorNedeff, Florin
dc.contributor.authorSandu, Ion
dc.contributor.authorMosnegutu, Emilian
dc.contributor.authorSandu, Andrei Victor
dc.contributor.authorLópez Ramírez, Juan Antonio 
dc.contributor.otherTecnologías del Medio Ambientees_ES
dc.date.accessioned2020-11-23T12:05:28Z
dc.date.available2020-11-23T12:05:28Z
dc.date.issued2020
dc.identifier.issn0034-7752
dc.identifier.urihttp://hdl.handle.net/10498/23971
dc.description.abstractThis paper presents a mathematical modeling for a series of experiments in which humic acid (AH) and calcium chloride (CaCl2) were used, in order to visualize the amount of contaminant before and after the nanofiltration (NF) process, using Excitation Emission Matrix Spectroscopy (EEMS). It allows to a better understanding of membrane fouling. The membrane used for these experiments was a NF ceramic membrane made of titanium dioxide (TiO2). For the experimental determinations, a constant amount of 10 mg/L HA and different amounts of CaCl2, respectively 1, 2, 3 and 4 mmol/L were used, considering the working methodology presented in this article. The presence of the amount of contaminant in water was determined using the EEMS method using the FP-8300 Spectrophotometer, after which a spectral analysis was performed. TableCurve 3D software was used to make the mathematical models in order to ensure that the equations obtained had the same shape. The values of the correlation coefficients, corresponding to the generated equations, have values ranging from 0.91 to 0.93. In order to verify the mathematical models thus obtained, graphs of the difference between the surface obtained with the help of the mathematical models and the surface obtained by means of real data were drawn. In conclusion, it turns out that, the largest difference was obtained in the case of samples taken from the feed, with a maximum difference of 31 fluorescence intensity arbitrary units (a.u.), and for the samples taken from the permeate the deference is 14 fluorescence intensity a.u.es_ES
dc.formatapplication/pdfes_ES
dc.language.isoenges_ES
dc.publisherSYSCOM 18 S.R.L.es_ES
dc.rightsAtribución 4.0 Internacional*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/*
dc.sourceRevista de Chimie (Rev. Chim.), Year 2020, Volume 71, Issue 5, 330-339es_ES
dc.subjectmathematical modelinges_ES
dc.subjectnanofiltration (NF)es_ES
dc.subjecthumic acid (HA)es_ES
dc.subjectcalcium chloride (CaCl2)es_ES
dc.subjectspectroscopyes_ES
dc.subjectemission excitation matrix (EEM)es_ES
dc.titleCeramic Nanofiltration Membrane Fouling: Application of Mathematical Modelling to the Use of Excitation Emission Matrix Spectroscopyes_ES
dc.typejournal articlees_ES
dc.rights.accessRightsopen accesses_ES
dc.identifier.doi10.37358/RC.20.5.8141


Ficheros en el ítem

Este ítem aparece en la(s) siguiente(s) colección(ones)

Mostrar el registro sencillo del ítem

Atribución 4.0 Internacional
Esta obra está bajo una Licencia Creative Commons Atribución 4.0 Internacional