NickelMaghrebV1, PascalFrancis, Corpus, bibRecord, 000136

Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies

Identifieur interne : 000136 ( PascalFrancis/Corpus ); précédent : 000135; suivant : 000137

Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies

Auteurs : N. Boujelben ; J. Bouzid ; Z. Elouear ; M. Feki

Source :

Environmental technology [ 0959-3330 ] ; 2010.

RBID : Pascal:11-0040300

Descripteurs français

Pascal (Inist)
- Rétention, Solution aqueuse, Cinétique, Condition opératoire, pH, Isotherme adsorption, Coefficient corrélation, Isotherme Langmuir, Modélisation, Sorption, Sorbant, Paramètre thermodynamique, Adsorption, Ordre 1, Ordre 2, Diffusion, Modèle cinétique, Captation, Désorption.

English descriptors

KwdEn :
- Adsorption, Adsorption isotherm, Aqueous solution, Correlation coefficient, Desorption, Diffusion, First order, Kinetic model, Kinetics, Langmuir isotherm, Modeling, Operating conditions, Retention, Second order, Sorbent, Sorption, Thermodynamic parameter, Uptake, pH.

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.

Notice en format standard (ISO 2709)

Pour connaître la documentation sur le format Inist Standard.

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A03		`1`		`@0 Environ. technol.`
A05				`@2 31`
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A08	`01`	`1`	`ENG`	`@1 Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies`
A11	`01`	`1`		`@1 BOUJELBEN (N.)`
A11	`02`	`1`		`@1 BOUZID (J.)`
A11	`03`	`1`		`@1 ELOUEAR (Z.)`
A11	`04`	`1`		`@1 FEKI (M.)`
A14	`01`			`@1 Laboratoire Eau Energie et Environnement, département de génie géologique, Ecole Nationale d'Ingénieurs de Sfax, BP W 3038 Sfax @3 TUN @Z 1 aut. @Z 2 aut. @Z 3 aut.`
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A20				`@1 1623-1634`
A21				`@1 2010`
A23	`01`			`@0 ENG`
A43	`01`			`@1 INIST @2 19606 @5 354000195035730130`
A44				`@0 0000 @1 © 2011 INIST-CNRS. All rights reserved.`
A45				`@0 45 ref.`
A47	`01`	`1`		`@0 11-0040300`
A60				`@1 P`
A61				`@0 A`
A64	`01`	`1`		`@0 Environmental technology`
A66	`01`			`@0 GBR`
C01	`01`		`ENG`	@0 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.
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C03	`01`	`X`	`ENG`	`@0 Retention @5 01`
C03	`01`	`X`	`SPA`	`@0 Retención @5 01`
C03	`02`	`X`	`FRE`	`@0 Solution aqueuse @5 02`
C03	`02`	`X`	`ENG`	`@0 Aqueous solution @5 02`
C03	`02`	`X`	`SPA`	`@0 Solución acuosa @5 02`
C03	`03`	`X`	`FRE`	`@0 Cinétique @5 03`
C03	`03`	`X`	`ENG`	`@0 Kinetics @5 03`
C03	`03`	`X`	`SPA`	`@0 Cinética @5 03`
C03	`04`	`X`	`FRE`	`@0 Condition opératoire @5 04`
C03	`04`	`X`	`ENG`	`@0 Operating conditions @5 04`
C03	`04`	`X`	`SPA`	`@0 Condición operatoria @5 04`
C03	`05`	`X`	`FRE`	`@0 pH @5 05`
C03	`05`	`X`	`ENG`	`@0 pH @5 05`
C03	`05`	`X`	`SPA`	`@0 pH @5 05`
C03	`06`	`X`	`FRE`	`@0 Isotherme adsorption @5 06`
C03	`06`	`X`	`ENG`	`@0 Adsorption isotherm @5 06`
C03	`06`	`X`	`SPA`	`@0 Isotermo adsorción @5 06`
C03	`07`	`X`	`FRE`	`@0 Coefficient corrélation @5 07`
C03	`07`	`X`	`ENG`	`@0 Correlation coefficient @5 07`
C03	`07`	`X`	`SPA`	`@0 Coeficiente correlación @5 07`
C03	`08`	`X`	`FRE`	`@0 Isotherme Langmuir @5 08`
C03	`08`	`X`	`ENG`	`@0 Langmuir isotherm @5 08`
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C03	`09`	`X`	`FRE`	`@0 Modélisation @5 09`
C03	`09`	`X`	`ENG`	`@0 Modeling @5 09`
C03	`09`	`X`	`SPA`	`@0 Modelización @5 09`
C03	`10`	`X`	`FRE`	`@0 Sorption @5 10`
C03	`10`	`X`	`ENG`	`@0 Sorption @5 10`
C03	`10`	`X`	`SPA`	`@0 Sorción @5 10`
C03	`11`	`X`	`FRE`	`@0 Sorbant @5 11`
C03	`11`	`X`	`ENG`	`@0 Sorbent @5 11`
C03	`11`	`X`	`SPA`	`@0 Sorbente @5 11`
C03	`12`	`X`	`FRE`	`@0 Paramètre thermodynamique @5 12`
C03	`12`	`X`	`ENG`	`@0 Thermodynamic parameter @5 12`
C03	`12`	`X`	`SPA`	`@0 Parámetro termodinámico @5 12`
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C03	`13`	`X`	`ENG`	`@0 Adsorption @5 13`
C03	`13`	`X`	`SPA`	`@0 Adsorción @5 13`
C03	`14`	`X`	`FRE`	`@0 Ordre 1 @5 14`
C03	`14`	`X`	`ENG`	`@0 First order @5 14`
C03	`14`	`X`	`SPA`	`@0 Orden 1 @5 14`
C03	`15`	`X`	`FRE`	`@0 Ordre 2 @5 15`
C03	`15`	`X`	`ENG`	`@0 Second order @5 15`
C03	`15`	`X`	`SPA`	`@0 Orden 2 @5 15`
C03	`16`	`X`	`FRE`	`@0 Diffusion @5 16`
C03	`16`	`X`	`ENG`	`@0 Diffusion @5 16`
C03	`16`	`X`	`SPA`	`@0 Difusión @5 16`
C03	`17`	`X`	`FRE`	`@0 Modèle cinétique @5 17`
C03	`17`	`X`	`ENG`	`@0 Kinetic model @5 17`
C03	`17`	`X`	`SPA`	`@0 Modelo cinético @5 17`
C03	`18`	`X`	`FRE`	`@0 Captation @5 18`
C03	`18`	`X`	`ENG`	`@0 Uptake @5 18`
C03	`18`	`X`	`SPA`	`@0 Captación @5 18`
C03	`19`	`X`	`FRE`	`@0 Désorption @5 19`
C03	`19`	`X`	`ENG`	`@0 Desorption @5 19`
C03	`19`	`X`	`SPA`	`@0 Desorción @5 19`
N21				`@1 024`
N44	`01`			`@1 OTO`
N82				`@1 OTO`

Format Inist (serveur)

NO :	PASCAL 11-0040300 INIST
ET :	Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies
AU :	BOUJELBEN (N.); BOUZID (J.); ELOUEAR (Z.); FEKI (M.)
AF :	Laboratoire Eau Energie et Environnement, département de génie géologique, Ecole Nationale d'Ingénieurs de Sfax, BP W 3038 Sfax/Tunisie (1 aut., 2 aut., 3 aut.); Unité de chimie industrielle I, Ecole Nationale d'Ingénieurs de Sfax, BP W 3038 Sfax/Tunisie (4 aut.)
DT :	Publication en série; Niveau analytique
SO :	Environmental technology; ISSN 0959-3330; Royaume-Uni; Da. 2010; Vol. 31; No. 14; Pp. 1623-1634; Bibl. 45 ref.
LA :	Anglais
EA :	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.
CC :	001D16; 001D07K
FD :	Rétention; Solution aqueuse; Cinétique; Condition opératoire; pH; Isotherme adsorption; Coefficient corrélation; Isotherme Langmuir; Modélisation; Sorption; Sorbant; Paramètre thermodynamique; Adsorption; Ordre 1; Ordre 2; Diffusion; Modèle cinétique; Captation; Désorption
ED :	Retention; Aqueous solution; Kinetics; Operating conditions; pH; Adsorption isotherm; Correlation coefficient; Langmuir isotherm; Modeling; Sorption; Sorbent; Thermodynamic parameter; Adsorption; First order; Second order; Diffusion; Kinetic model; Uptake; Desorption
SD :	Retención; Solución acuosa; Cinética; Condición operatoria; pH; Isotermo adsorción; Coeficiente correlación; Isoterma Langmuir; Modelización; Sorción; Sorbente; Parámetro termodinámico; Adsorción; Orden 1; Orden 2; Difusión; Modelo cinético; Captación; Desorción
LO :	INIST-19606.354000195035730130
ID :	11-0040300

Links to Exploration step

Pascal:11-0040300

Le document en format XML

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<term>Second order</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>
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<fA14 i1="01"><s1>Laboratoire Eau Energie et Environnement, département de génie géologique, Ecole Nationale d'Ingénieurs de Sfax, BP W 3038 Sfax</s1>
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<fA14 i1="02"><s1>Unité de chimie industrielle I, Ecole Nationale d'Ingénieurs de Sfax, BP W 3038 Sfax</s1>
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<fC01 i1="01" l="ENG"><s0>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.</s0>
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<s5>03</s5>
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<s5>03</s5>
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<fC03 i1="04" i2="X" l="FRE"><s0>Condition opératoire</s0>
<s5>04</s5>
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<fC03 i1="04" i2="X" l="ENG"><s0>Operating conditions</s0>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Condición operatoria</s0>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>pH</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>pH</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>pH</s0>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Isotherme adsorption</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Adsorption isotherm</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Isotermo adsorción</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Coefficient corrélation</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Correlation coefficient</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Coeficiente correlación</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Isotherme Langmuir</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Langmuir isotherm</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Isoterma Langmuir</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Modélisation</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Modeling</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Modelización</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Sorption</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Sorption</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Sorción</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Sorbant</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Sorbent</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Sorbente</s0>
<s5>11</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Paramètre thermodynamique</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Thermodynamic parameter</s0>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Parámetro termodinámico</s0>
<s5>12</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Adsorption</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Adsorption</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Adsorción</s0>
<s5>13</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Ordre 1</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>First order</s0>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Orden 1</s0>
<s5>14</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Ordre 2</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Second order</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Orden 2</s0>
<s5>15</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE"><s0>Diffusion</s0>
<s5>16</s5>
</fC03>
<fC03 i1="16" i2="X" l="ENG"><s0>Diffusion</s0>
<s5>16</s5>
</fC03>
<fC03 i1="16" i2="X" l="SPA"><s0>Difusión</s0>
<s5>16</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Modèle cinétique</s0>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Kinetic model</s0>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Modelo cinético</s0>
<s5>17</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE"><s0>Captation</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="ENG"><s0>Uptake</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="SPA"><s0>Captación</s0>
<s5>18</s5>
</fC03>
<fC03 i1="19" i2="X" l="FRE"><s0>Désorption</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="ENG"><s0>Desorption</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="SPA"><s0>Desorción</s0>
<s5>19</s5>
</fC03>
<fN21><s1>024</s1>
</fN21>
<fN44 i1="01"><s1>OTO</s1>
</fN44>
<fN82><s1>OTO</s1>
</fN82>
</pA>
</standard>
<server><NO>PASCAL 11-0040300 INIST</NO>
<ET>Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies</ET>
<AU>BOUJELBEN (N.); BOUZID (J.); ELOUEAR (Z.); FEKI (M.)</AU>
<AF>Laboratoire Eau Energie et Environnement, département de génie géologique, Ecole Nationale d'Ingénieurs de Sfax, BP W 3038 Sfax/Tunisie (1 aut., 2 aut., 3 aut.); Unité de chimie industrielle I, Ecole Nationale d'Ingénieurs de Sfax, BP W 3038 Sfax/Tunisie (4 aut.)</AF>
<DT>Publication en série; Niveau analytique</DT>
<SO>Environmental technology; ISSN 0959-3330; Royaume-Uni; Da. 2010; Vol. 31; No. 14; Pp. 1623-1634; Bibl. 45 ref.</SO>
<LA>Anglais</LA>
<EA>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.</EA>
<CC>001D16; 001D07K</CC>
<FD>Rétention; Solution aqueuse; Cinétique; Condition opératoire; pH; Isotherme adsorption; Coefficient corrélation; Isotherme Langmuir; Modélisation; Sorption; Sorbant; Paramètre thermodynamique; Adsorption; Ordre 1; Ordre 2; Diffusion; Modèle cinétique; Captation; Désorption</FD>
<ED>Retention; Aqueous solution; Kinetics; Operating conditions; pH; Adsorption isotherm; Correlation coefficient; Langmuir isotherm; Modeling; Sorption; Sorbent; Thermodynamic parameter; Adsorption; First order; Second order; Diffusion; Kinetic model; Uptake; Desorption</ED>
<SD>Retención; Solución acuosa; Cinética; Condición operatoria; pH; Isotermo adsorción; Coeficiente correlación; Isoterma Langmuir; Modelización; Sorción; Sorbente; Parámetro termodinámico; Adsorción; Orden 1; Orden 2; Difusión; Modelo cinético; Captación; Desorción</SD>
<LO>INIST-19606.354000195035730130</LO>
<ID>11-0040300</ID>
</server>
</inist>
</record>

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	Serveur d'exploration sur le nickel au Maghreb
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Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies

Retention of nickel from aqueous solutions using iron oxide and manganese oxide coated sand: kinetic and thermodynamic studies

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