NickelMaghrebV1, PascalFrancis, Curation, bibRecord, 000388

Removal of heavy metals from aqueous solutions by Algerian bentonite

Identifieur interne : 000388 ( PascalFrancis/Curation ); précédent : 000387; suivant : 000389

Removal of heavy metals from aqueous solutions by Algerian bentonite

Auteurs : F. Mohammed-Azizi [Algérie] ; S. Dib [Algérie] ; M. Boufatit [Algérie]

Source :

Desalination and water treatment : (Print) [ 1944-3994 ] ; 2013.

RBID : Pascal:13-0265125

Descripteurs français

Pascal (Inist)
- Cuivre II Composé, Métal lourd, Epuration eau usée, Algérie, Bentonite, Argile, Eau usée industrielle, Epuration physicochimique, Cinétique, Zinc II Composé, Adsorption, Plomb II Composé, Adsorbant, Nickel II Composé, Microscopie électronique balayage, Aire surface spécifique, Caractérisation, Diffraction RX, Isotherme adsorption, Structure surface, Morphologie, Spectrométrie IR, Transformation Fourier, Propriété surface, FT IR.
Wicri :
- geographic : Algérie.
- topic : Métal lourd.

English descriptors

KwdEn :
- Adsorbent, Adsorption, Adsorption isotherm, Algeria, Bentonite, Characterization, Clay, Copper II Compounds, Fourier transformation, Heavy metal, Industrial waste water, Infrared spectrometry, Kinetics, Lead II Compounds, Morphology, Nickel II Compounds, Physicochemical purification, Scanning electron microscopy, Specific surface area, Surface properties, Surface structure, Waste water purification, X ray diffraction, Zinc II Compounds.

Abstract

This study aimed the removal of heavy metals by Algerian bentonite. An Algerian natural clay, a bentonite of Mostaganem (N.W. Algeria), has been first acid-activated (HCl) and characterized by powder X-ray diffraction, FT-IR spectroscopy, electron microscopy (SEM), and specific surface area. The acid-activated clay (AAC) was employed as adsorbent for the removal of Zn²⁺, Pb²⁺, Cu²⁺, and Ni²⁺ ions from aqueous solutions using adsorption method. The sorption process was examined in terms of its equilibrium and kinetics. The study was carried out by varying shaking time, pH, concentration of metal ions and amount of adsorbent. The optimum parameters of our study obtained were pH values range (4-6), mass of AAC (1 g), shaking time (1 h), and initial concentration of metal ions (10 mgL^-1). The results have shown that Algerian bentonite clay had significant potential for removing Zn²⁺, Pb²⁺, Cu²⁺, and Ni²⁺ ions from polluted water.

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A09	`01`	`1`	`ENG`	`@1 Papers presented at the Conference on Membranes in Drinking and Industrial Water Treatment-MDIW 2010, June 27-30, 2010, Trondheim, Norway`
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C01	`01`		`ENG`	@0 This study aimed the removal of heavy metals by Algerian bentonite. An Algerian natural clay, a bentonite of Mostaganem (N.W. Algeria), has been first acid-activated (HCl) and characterized by powder X-ray diffraction, FT-IR spectroscopy, electron microscopy (SEM), and specific surface area. The acid-activated clay (AAC) was employed as adsorbent for the removal of Zn²⁺, Pb²⁺, Cu²⁺, and Ni²⁺ ions from aqueous solutions using adsorption method. The sorption process was examined in terms of its equilibrium and kinetics. The study was carried out by varying shaking time, pH, concentration of metal ions and amount of adsorbent. The optimum parameters of our study obtained were pH values range (4-6), mass of AAC (1 g), shaking time (1 h), and initial concentration of metal ions (10 mgL^-1). The results have shown that Algerian bentonite clay had significant potential for removing Zn²⁺, Pb²⁺, Cu²⁺, and Ni²⁺ ions from polluted water.
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C03	`05`	`X`	`FRE`	`@0 Bentonite @5 05`
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N21				`@1 252`

A30	`01`	`1`	`ENG`	`@1 Membranes in Drinking and Industrial Water Treatment-MDIW Conference @3 Trondheim NOR @4 2010-06-27`

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Pascal:13-0265125

Le document en format XML

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<affiliation wicri:level="1"><inist:fA14 i1="01"><s1>Faculté de Chimie, Laboratoire d'Electrochimie-Corrosion, Métallurgie et Chimie Minérale, Université des Sciences et de la Technologie Houari Boumediène (U. S. T. H. B.), B.P.: 32, El-Alia, Bab-Ezzouar</s1>
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<term>Copper II Compounds</term>
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<term>Heavy metal</term>
<term>Industrial waste water</term>
<term>Infrared spectrometry</term>
<term>Kinetics</term>
<term>Lead II Compounds</term>
<term>Morphology</term>
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<term>Physicochemical purification</term>
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<term>Epuration physicochimique</term>
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<term>Zinc II Composé</term>
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<front><div type="abstract" xml:lang="en">This study aimed the removal of heavy metals by Algerian bentonite. An Algerian natural clay, a bentonite of Mostaganem (N.W. Algeria), has been first acid-activated (HCl) and characterized by powder X-ray diffraction, FT-IR spectroscopy, electron microscopy (SEM), and specific surface area. The acid-activated clay (AAC) was employed as adsorbent for the removal of Zn<sup>2+</sup>
, Pb<sup>2+</sup>
, Cu<sup>2+</sup>
, and Ni<sup>2+</sup>
 ions from aqueous solutions using adsorption method. The sorption process was examined in terms of its equilibrium and kinetics. The study was carried out by varying shaking time, pH, concentration of metal ions and amount of adsorbent. The optimum parameters of our study obtained were pH values range (4-6), mass of AAC (1 g), shaking time (1 h), and initial concentration of metal ions (10 mgL<sup>-1</sup>
). The results have shown that Algerian bentonite clay had significant potential for removing Zn<sup>2+</sup>
, Pb<sup>2+</sup>
, Cu<sup>2+</sup>
, and Ni<sup>2+</sup>
 ions from polluted water.</div>
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<fC01 i1="01" l="ENG"><s0>This study aimed the removal of heavy metals by Algerian bentonite. An Algerian natural clay, a bentonite of Mostaganem (N.W. Algeria), has been first acid-activated (HCl) and characterized by powder X-ray diffraction, FT-IR spectroscopy, electron microscopy (SEM), and specific surface area. The acid-activated clay (AAC) was employed as adsorbent for the removal of Zn<sup>2+</sup>
, Pb<sup>2+</sup>
, Cu<sup>2+</sup>
, and Ni<sup>2+</sup>
 ions from aqueous solutions using adsorption method. The sorption process was examined in terms of its equilibrium and kinetics. The study was carried out by varying shaking time, pH, concentration of metal ions and amount of adsorbent. The optimum parameters of our study obtained were pH values range (4-6), mass of AAC (1 g), shaking time (1 h), and initial concentration of metal ions (10 mgL<sup>-1</sup>
). The results have shown that Algerian bentonite clay had significant potential for removing Zn<sup>2+</sup>
, Pb<sup>2+</sup>
, Cu<sup>2+</sup>
, and Ni<sup>2+</sup>
 ions from polluted water.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001D16A05B</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Cuivre II Composé</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Copper II Compounds</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Cobre II Compuesto</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Métal lourd</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Heavy metal</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Metal pesado</s0>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Epuration eau usée</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Waste water purification</s0>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Depuración aguas servidas</s0>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Algérie</s0>
<s2>NG</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Algeria</s0>
<s2>NG</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Argelia</s0>
<s2>NG</s2>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Bentonite</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Bentonite</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Bentonita</s0>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Argile</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Clay</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Arcilla</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Eau usée industrielle</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Industrial waste water</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Agua servida industrial</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Epuration physicochimique</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Physicochemical purification</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Depuración fisicoquímica</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Cinétique</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Kinetics</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Cinética</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Zinc II Composé</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Zinc II Compounds</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Zinc II Compuesto</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Adsorption</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Adsorption</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Adsorción</s0>
<s5>11</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Plomb II Composé</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Lead II Compounds</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>12</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Plomo II Compuesto</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>12</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Adsorbant</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Adsorbent</s0>
<s5>13</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Adsorbente</s0>
<s5>13</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Nickel II Composé</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Nickel II Compounds</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>14</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Niquel II Compuesto</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>14</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Microscopie électronique balayage</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Scanning electron microscopy</s0>
<s5>15</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Microscopía electrónica barrido</s0>
<s5>15</s5>
</fC03>
<fC03 i1="16" i2="3" l="FRE"><s0>Aire surface spécifique</s0>
<s5>16</s5>
</fC03>
<fC03 i1="16" i2="3" l="ENG"><s0>Specific surface area</s0>
<s5>16</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Caractérisation</s0>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Characterization</s0>
<s5>17</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Caracterización</s0>
<s5>17</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE"><s0>Diffraction RX</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="ENG"><s0>X ray diffraction</s0>
<s5>18</s5>
</fC03>
<fC03 i1="18" i2="X" l="SPA"><s0>Difracción RX</s0>
<s5>18</s5>
</fC03>
<fC03 i1="19" i2="X" l="FRE"><s0>Isotherme adsorption</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="ENG"><s0>Adsorption isotherm</s0>
<s5>19</s5>
</fC03>
<fC03 i1="19" i2="X" l="SPA"><s0>Isotermo adsorción</s0>
<s5>19</s5>
</fC03>
<fC03 i1="20" i2="X" l="FRE"><s0>Structure surface</s0>
<s5>32</s5>
</fC03>
<fC03 i1="20" i2="X" l="ENG"><s0>Surface structure</s0>
<s5>32</s5>
</fC03>
<fC03 i1="20" i2="X" l="SPA"><s0>Estructura superficie</s0>
<s5>32</s5>
</fC03>
<fC03 i1="21" i2="X" l="FRE"><s0>Morphologie</s0>
<s5>33</s5>
</fC03>
<fC03 i1="21" i2="X" l="ENG"><s0>Morphology</s0>
<s5>33</s5>
</fC03>
<fC03 i1="21" i2="X" l="SPA"><s0>Morfología</s0>
<s5>33</s5>
</fC03>
<fC03 i1="22" i2="X" l="FRE"><s0>Spectrométrie IR</s0>
<s5>34</s5>
</fC03>
<fC03 i1="22" i2="X" l="ENG"><s0>Infrared spectrometry</s0>
<s5>34</s5>
</fC03>
<fC03 i1="22" i2="X" l="SPA"><s0>Espectrometría IR</s0>
<s5>34</s5>
</fC03>
<fC03 i1="23" i2="X" l="FRE"><s0>Transformation Fourier</s0>
<s5>35</s5>
</fC03>
<fC03 i1="23" i2="X" l="ENG"><s0>Fourier transformation</s0>
<s5>35</s5>
</fC03>
<fC03 i1="23" i2="X" l="SPA"><s0>Transformación Fourier</s0>
<s5>35</s5>
</fC03>
<fC03 i1="24" i2="X" l="FRE"><s0>Propriété surface</s0>
<s5>36</s5>
</fC03>
<fC03 i1="24" i2="X" l="ENG"><s0>Surface properties</s0>
<s5>36</s5>
</fC03>
<fC03 i1="24" i2="X" l="SPA"><s0>Propiedad superficie</s0>
<s5>36</s5>
</fC03>
<fC03 i1="25" i2="X" l="FRE"><s0>FT IR</s0>
<s4>INC</s4>
<s5>76</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE"><s0>Afrique</s0>
<s2>NG</s2>
</fC07>
<fC07 i1="01" i2="X" l="ENG"><s0>Africa</s0>
<s2>NG</s2>
</fC07>
<fC07 i1="01" i2="X" l="SPA"><s0>Africa</s0>
<s2>NG</s2>
</fC07>
<fC07 i1="02" i2="X" l="FRE"><s0>Elément trace</s0>
<s5>53</s5>
</fC07>
<fC07 i1="02" i2="X" l="ENG"><s0>Trace element</s0>
<s5>53</s5>
</fC07>
<fC07 i1="02" i2="X" l="SPA"><s0>Elemento traza</s0>
<s5>53</s5>
</fC07>
<fN21><s1>252</s1>
</fN21>
</pA>
<pR><fA30 i1="01" i2="1" l="ENG"><s1>Membranes in Drinking and Industrial Water Treatment-MDIW Conference</s1>
<s3>Trondheim NOR</s3>
<s4>2010-06-27</s4>
</fA30>
</pR>
</standard>
</inist>
</record>

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	Serveur d'exploration sur le nickel au Maghreb
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Serveur d'exploration sur le nickel au Maghreb

Removal of heavy metals from aqueous solutions by Algerian bentonite

Removal of heavy metals from aqueous solutions by Algerian bentonite

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