Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies
Identifieur interne : 000412 ( Main/Exploration ); précédent : 000411; suivant : 000413Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies
Auteurs : N. Boujelben [Tunisie] ; J. Bouzid [Tunisie] ; Z. Elouear [Tunisie] ; M. Feki [Tunisie]Source :
- Environmental technology [ 0959-3330 ] ; 2010.
Descripteurs français
- Pascal (Inist)
English descriptors
- KwdEn :
- Absorption, Adsorption, Adsorption isotherm, Aqueous solution, Computer Simulation, Correlation coefficient, Desorption, Diffusion, Ferric Compounds (chemistry), First order, Kinetic model, Kinetics, Langmuir isotherm, Manganese Compounds (chemistry), Modeling, Models, Chemical, Nickel (chemistry), Nickel (isolation & purification), Operating conditions, Oxides (chemistry), Retention, Second order, Soil (chemistry), Sorbent, Sorption, Thermodynamic parameter, Thermodynamics, Ultrafiltration (methods), Uptake, Water Pollutants, Chemical (chemistry), Water Pollutants, Chemical (isolation & purification), Water Purification (methods), pH.
- MESH :
- chemical , chemistry : Ferric Compounds, Manganese Compounds, Nickel, Oxides, Soil, Water Pollutants, Chemical.
- chemical , isolation & purification : Nickel, Water Pollutants, Chemical.
- methods : Ultrafiltration, Water Purification.
- Absorption, Computer Simulation, Kinetics, Models, Chemical, Thermodynamics.
Abstract
In this study, the removal of nickel ions from aqueous solutions using iron oxide and manganese oxide coated sand (ICS and MCS) under different experimental conditions was investigated. The effect of metal concentration, contact time, solution pH and temperature on the amount of Ni(II) sorbed was studied and discussed. Langmuir and Freundlich isotherm constants and correlation coefficients for the present systems at different temperatures were calculated and compared. The equilibrium process was well described by the Langmuir isotherm model: the maximum sorption capacities (at 29 K) were 2.73 mg Ni/g and 3.33 mg Ni/g of sorbent for ICS and MCS, respectively. Isotherms were also used to evaluate the thermodynamic parameters (ΔG°, ΔH°, ΔS°) of adsorption. The sorption kinetics were tested for the pseudo-first-order, pseudo-second-order and intra-particle diffusion models. Good correlation coefficients were obtained for the pseudo-second-order kinetic model, showing that the nickel uptake process followed the pseudo-second-order rate expression.
Affiliations:
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Le document en format XML
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<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Absorption</term>
<term>Adsorption</term>
<term>Adsorption isotherm</term>
<term>Aqueous solution</term>
<term>Computer Simulation</term>
<term>Correlation coefficient</term>
<term>Desorption</term>
<term>Diffusion</term>
<term>Ferric Compounds (chemistry)</term>
<term>First order</term>
<term>Kinetic model</term>
<term>Kinetics</term>
<term>Langmuir isotherm</term>
<term>Manganese Compounds (chemistry)</term>
<term>Modeling</term>
<term>Models, Chemical</term>
<term>Nickel (chemistry)</term>
<term>Nickel (isolation & purification)</term>
<term>Operating conditions</term>
<term>Oxides (chemistry)</term>
<term>Retention</term>
<term>Second order</term>
<term>Soil (chemistry)</term>
<term>Sorbent</term>
<term>Sorption</term>
<term>Thermodynamic parameter</term>
<term>Thermodynamics</term>
<term>Ultrafiltration (methods)</term>
<term>Uptake</term>
<term>Water Pollutants, Chemical (chemistry)</term>
<term>Water Pollutants, Chemical (isolation & purification)</term>
<term>Water Purification (methods)</term>
<term>pH</term>
</keywords>
<keywords scheme="MESH" type="chemical" qualifier="chemistry" xml:lang="en"><term>Ferric Compounds</term>
<term>Manganese Compounds</term>
<term>Nickel</term>
<term>Oxides</term>
<term>Soil</term>
<term>Water Pollutants, Chemical</term>
</keywords>
<keywords scheme="MESH" type="chemical" qualifier="isolation & purification" xml:lang="en"><term>Nickel</term>
<term>Water Pollutants, Chemical</term>
</keywords>
<keywords scheme="MESH" qualifier="methods" xml:lang="en"><term>Ultrafiltration</term>
<term>Water Purification</term>
</keywords>
<keywords scheme="MESH" xml:lang="en"><term>Absorption</term>
<term>Computer Simulation</term>
<term>Kinetics</term>
<term>Models, Chemical</term>
<term>Thermodynamics</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Rétention</term>
<term>Solution aqueuse</term>
<term>Cinétique</term>
<term>Condition opératoire</term>
<term>pH</term>
<term>Isotherme adsorption</term>
<term>Coefficient corrélation</term>
<term>Isotherme Langmuir</term>
<term>Modélisation</term>
<term>Sorption</term>
<term>Sorbant</term>
<term>Paramètre thermodynamique</term>
<term>Adsorption</term>
<term>Ordre 1</term>
<term>Ordre 2</term>
<term>Diffusion</term>
<term>Modèle cinétique</term>
<term>Captation</term>
<term>Désorption</term>
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<front><div type="abstract" xml:lang="en">In this study, the removal of nickel ions from aqueous solutions using iron oxide and manganese oxide coated sand (ICS and MCS) under different experimental conditions was investigated. The effect of metal concentration, contact time, solution pH and temperature on the amount of Ni(II) sorbed was studied and discussed. Langmuir and Freundlich isotherm constants and correlation coefficients for the present systems at different temperatures were calculated and compared. The equilibrium process was well described by the Langmuir isotherm model: the maximum sorption capacities (at 29 K) were 2.73 mg Ni/g and 3.33 mg Ni/g of sorbent for ICS and MCS, respectively. Isotherms were also used to evaluate the thermodynamic parameters (ΔG°, ΔH°, ΔS°) of adsorption. The sorption kinetics were tested for the pseudo-first-order, pseudo-second-order and intra-particle diffusion models. Good correlation coefficients were obtained for the pseudo-second-order kinetic model, showing that the nickel uptake process followed the pseudo-second-order rate expression.</div>
</front>
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<affiliations><list><country><li>Tunisie</li>
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<tree><country name="Tunisie"><noRegion><name sortKey="Boujelben, N" sort="Boujelben, N" uniqKey="Boujelben N" first="N." last="Boujelben">N. Boujelben</name>
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<name sortKey="Bouzid, J" sort="Bouzid, J" uniqKey="Bouzid J" first="J." last="Bouzid">J. Bouzid</name>
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<name sortKey="Feki, M" sort="Feki, M" uniqKey="Feki M" first="M." last="Feki">M. Feki</name>
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