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Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device

Nickel (II) preconcentration and speciation analysis using a hollow fiber supported liquid membrane (HFSLM) device was studied. A counterflow of protons coupled to complexation with formate provided the driving force of the process, while Kelex 100 was employed as carrier. The influence of variables...

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Autores principales: Bautista-Flores, Ana Nelly, de San Miguel, Eduardo Rodríguez, de Gyves, Josefina, Jönsson, Jan Åke
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2011
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4021897/
https://www.ncbi.nlm.nih.gov/pubmed/24957733
http://dx.doi.org/10.3390/membranes1030217
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author Bautista-Flores, Ana Nelly
de San Miguel, Eduardo Rodríguez
de Gyves, Josefina
Jönsson, Jan Åke
author_facet Bautista-Flores, Ana Nelly
de San Miguel, Eduardo Rodríguez
de Gyves, Josefina
Jönsson, Jan Åke
author_sort Bautista-Flores, Ana Nelly
collection PubMed
description Nickel (II) preconcentration and speciation analysis using a hollow fiber supported liquid membrane (HFSLM) device was studied. A counterflow of protons coupled to complexation with formate provided the driving force of the process, while Kelex 100 was employed as carrier. The influence of variables related to module configuration (acceptor pH and carrier concentration) and to the sample properties (donor pH) on the preconcentration factor, E, was simultaneously studied and optimized using a 3 factor Doehlert matrix response surface methodology. The effect of metal concentration was studied as well. Preconcentration factors as high as 4240 were observed depending on the values of the different variables. The effects of the presence of inorganic anions (NO(2)(−), SO(4)(2−), Cl(−), NO(3)(−), CO(3)(2−), CN(−)) and dissolved organic matter (DOM) in the form of humic acids were additionally considered in order to carry out a speciation analysis study. Nickel preconcentration was observed to be independent of both effects, except when cyanide was present in the donor phase. A characterization of the transport regime was performed through the analysis of the dependence of E on the temperature. E increases with the increase in temperature according to the equation E(K) = −8617.3 + 30.5T with an activation energy of 56.7 kJ mol(−1) suggesting a kinetic-controlled regime. Sample depletion ranged from 12 to 1.2% depending on the volume of the donor phase (100 to 1000 mL, respectively).
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spelling pubmed-40218972014-05-27 Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device Bautista-Flores, Ana Nelly de San Miguel, Eduardo Rodríguez de Gyves, Josefina Jönsson, Jan Åke Membranes (Basel) Article Nickel (II) preconcentration and speciation analysis using a hollow fiber supported liquid membrane (HFSLM) device was studied. A counterflow of protons coupled to complexation with formate provided the driving force of the process, while Kelex 100 was employed as carrier. The influence of variables related to module configuration (acceptor pH and carrier concentration) and to the sample properties (donor pH) on the preconcentration factor, E, was simultaneously studied and optimized using a 3 factor Doehlert matrix response surface methodology. The effect of metal concentration was studied as well. Preconcentration factors as high as 4240 were observed depending on the values of the different variables. The effects of the presence of inorganic anions (NO(2)(−), SO(4)(2−), Cl(−), NO(3)(−), CO(3)(2−), CN(−)) and dissolved organic matter (DOM) in the form of humic acids were additionally considered in order to carry out a speciation analysis study. Nickel preconcentration was observed to be independent of both effects, except when cyanide was present in the donor phase. A characterization of the transport regime was performed through the analysis of the dependence of E on the temperature. E increases with the increase in temperature according to the equation E(K) = −8617.3 + 30.5T with an activation energy of 56.7 kJ mol(−1) suggesting a kinetic-controlled regime. Sample depletion ranged from 12 to 1.2% depending on the volume of the donor phase (100 to 1000 mL, respectively). MDPI 2011-08-18 /pmc/articles/PMC4021897/ /pubmed/24957733 http://dx.doi.org/10.3390/membranes1030217 Text en © 2011 by the authors; licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution license (http://creativecommons.org/licenses/by/3.0/).
spellingShingle Article
Bautista-Flores, Ana Nelly
de San Miguel, Eduardo Rodríguez
de Gyves, Josefina
Jönsson, Jan Åke
Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device
title Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device
title_full Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device
title_fullStr Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device
title_full_unstemmed Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device
title_short Nickel (II) Preconcentration and Speciation Analysis During Transport from Aqueous Solutions Using a Hollow-fiber Permeation Liquid Membrane (HFPLM) Device
title_sort nickel (ii) preconcentration and speciation analysis during transport from aqueous solutions using a hollow-fiber permeation liquid membrane (hfplm) device
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4021897/
https://www.ncbi.nlm.nih.gov/pubmed/24957733
http://dx.doi.org/10.3390/membranes1030217
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