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    <title>NISCAIR Online Periodicals Repository Collection: IJCT Vol.18(5) [September 2011]</title>
    <link>http://nopr.niscair.res.in/handle/123456789/13007</link>
    <description />
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        <rdf:li resource="http://nopr.niscair.res.in/handle/123456789/13036" />
        <rdf:li resource="http://nopr.niscair.res.in/handle/123456789/13035" />
        <rdf:li resource="http://nopr.niscair.res.in/handle/123456789/13034" />
        <rdf:li resource="http://nopr.niscair.res.in/handle/123456789/13033" />
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  <item rdf:about="http://nopr.niscair.res.in/handle/123456789/13036">
    <title>Removal of Ni (II) from aqueous solutions by adsorption onto &lt;i style=""&gt;Cajanus cajan L &lt;/i&gt;Milsp seed shell activated carbons</title>
    <link>http://nopr.niscair.res.in/handle/123456789/13036</link>
    <description>Title: Removal of Ni (II) from aqueous solutions by adsorption onto &lt;i style=""&gt;Cajanus cajan L &lt;/i&gt;Milsp seed shell activated carbons
&lt;br/&gt;
&lt;br/&gt;Authors: Thamilarasu, P; Sivakumar, P; Karunakaran, K
&lt;br/&gt;
&lt;br/&gt;Abstract: The&#xD;
adsorptive removal of Ni(II) from aqueous solution using &lt;i&gt;Cajanus cajan L &lt;/i&gt;Milsp&#xD;
seed shells activated carbon (CCC) and polypyrrole coated &lt;i&gt;Cajanus cajan L &lt;/i&gt;Milsp&#xD;
seed shells activated carbon (PPy/CCC) has been carried out under various&#xD;
experimental conditions. Quantity of Ni(II) uptake at&#xD;
50 mg of activated carbon is 25.75 mg/g for CCC and 29.60 mg/g for PPy/CCC.&#xD;
Adsorption data are modeled with Freundlich, Langmuir and Temkin adsorption&#xD;
isotherms. Thermodynamics parameters, such as &lt;img src='/image/spc_char/delta.gif' border=0&gt;H&lt;sup&gt;o&lt;/sup&gt;, &lt;img src='/image/spc_char/delta.gif' border=0&gt;S&lt;sup&gt;o&lt;/sup&gt;,&#xD;
and &lt;img src='/image/spc_char/delta.gif' border=0&gt;G&lt;sup&gt;o &lt;/sup&gt;have been calculated and the findings indicate that the&#xD;
adsorption is spontaneous and endothermic. Enthalpy change values range from&#xD;
8.90 kJ/mol to 23.04 kJ/mol, and based on these values the adsorption of Ni(II)&#xD;
by CCC could be a physisorption. A mechanism involving intra particle diffusion&#xD;
and surface adsorption has been proposed for the adsorption of Ni(II) onto the&#xD;
adsorbent. Adsorbent used in this study is also characterized by FT-IR and SEM&#xD;
before and after the adsorption of metal ions.
&lt;br/&gt;
&lt;br/&gt;Page(s): 414-420</description>
  </item>
  <item rdf:about="http://nopr.niscair.res.in/handle/123456789/13035">
    <title>Removal of arsenic ions and bacteriological contamination from aqueous solutions using chitosan nanospheres</title>
    <link>http://nopr.niscair.res.in/handle/123456789/13035</link>
    <description>Title: Removal of arsenic ions and bacteriological contamination from aqueous solutions using chitosan nanospheres
&lt;br/&gt;
&lt;br/&gt;Authors: Singh, P; Bajpai, J; Bajpai, A K; Shrivastava, R B
&lt;br/&gt;
&lt;br/&gt;Abstract: This paper reports study on the&#xD;
removal of As (V) by chitosan nanospheres following batch studies conducted as&#xD;
a function of dosage, contact time and temperature. The kinetic investigation&#xD;
of the removal process reveals that the uptake of As (V) ions by chitosan is&#xD;
very rapid in the first 40 min and then an equilibrium adsorption is achieved&#xD;
in next 20 min. The adsorption data has been applied to Langmuir and Freundlich&#xD;
isotherm equations and various experimental parameters such as solid to liquid&#xD;
ratio, &lt;i style=""&gt;p&lt;/i&gt;H, temperature and contact&#xD;
time are varied to optimize the conditions for the removal of arsenic ions.&#xD;
Antibacterial studies are also performed on native chitosan and silver&#xD;
nanoparticles loaded chitosan nanospheres and dissolved oxygen is calculated in&#xD;
water samples treated with chitosan and Ag-chitosan nanospheres. &lt;i style=""&gt;Escherichia coli&lt;/i&gt; is used to test the&#xD;
bactericidal efficacy of synthesized Ag-chitosan nanospheres. These nanospheres&#xD;
are found to have significantly higher antibacterial activity than the native&#xD;
chitosan nanospheres.
&lt;br/&gt;
&lt;br/&gt;Page(s): 403-413</description>
  </item>
  <item rdf:about="http://nopr.niscair.res.in/handle/123456789/13034">
    <title>Hexavalent chromium removal by gingelly oil cake carbon  activated with zinc chloride</title>
    <link>http://nopr.niscair.res.in/handle/123456789/13034</link>
    <description>Title: Hexavalent chromium removal by gingelly oil cake carbon  activated with zinc chloride
&lt;br/&gt;
&lt;br/&gt;Authors: Nagashanmugam, K B; Srinivasan, K
&lt;br/&gt;
&lt;br/&gt;Abstract: An activated carbon has been prepared from&#xD;
gingelly oil cake (GOC) by zinc chloride treatment and its Cr(VI) removal&#xD;
capacity is compared with that of commercial activated carbon (CAC). The effect&#xD;
of experimental parameters such as &lt;i&gt;p&lt;/i&gt;H, initial concentration, contact&#xD;
time and adsorbents dose for Cr(VI) removal has been studied. Langmuir,&#xD;
Freundlich and Temkin models are tested to describe the equilibrium isotherms.&#xD;
The maximum adsorption capacity of the adsorbents calculated from Langmuir&#xD;
isotherm is found to be 62.5 mg/g and 25.13 mg/g for zinc chloride treated&#xD;
gingelly oil cake carbon (ZTGOC) and CAC respectively. R&lt;sup&gt;2&lt;/sup&gt; values&#xD;
show that both Langmuir and Freundlich models fit well to explain the&#xD;
adsorption phenomenon for ZTGOC and CAC. The kinetic data fits best to pseudo-second&#xD;
order model. FT-IR analysis has been used to obtain information on the nature&#xD;
of possible interaction between carbon adsorbents and metal ions. SEM images&#xD;
confirm the adsorption of Cr(VI) onto these adsorbents through morphological&#xD;
observations. Thermodynamic study shows the feasibility of process and&#xD;
spontaneous nature of the adsorption. The carbon adsorbents have also been tested&#xD;
for the removal of Cr(VI) from chrome plating wastewater and &amp;nbsp;are found to remove Cr(VI) effectively.&lt;i style=""&gt;&lt;/i&gt;
&lt;br/&gt;
&lt;br/&gt;Page(s): 391-402</description>
  </item>
  <item rdf:about="http://nopr.niscair.res.in/handle/123456789/13033">
    <title>Influence of &lt;i&gt;Ficus religiosa&lt;/i&gt; leaf powder on bisorption of cobalt</title>
    <link>http://nopr.niscair.res.in/handle/123456789/13033</link>
    <description>Title: Influence of &lt;i&gt;Ficus religiosa&lt;/i&gt; leaf powder on bisorption of cobalt
&lt;br/&gt;
&lt;br/&gt;Authors: Krishna, B; Venkateswarlu, P
&lt;br/&gt;
&lt;br/&gt;Abstract: The batch-wise biosorption of cobalt by &lt;i style=""&gt;Ficus&#xD;
religiosa&lt;/i&gt; (peepul) leaf powder has been carried out. The optimum&#xD;
biosorbent dosage is 60 g/L for an equilibrium agitation time of 90 min. Percentage&#xD;
removal of cobalt is increased from 70.9 to 97.2 (0.96 to 1.45 mg/g) with&#xD;
decrease in acidity in the &lt;i style=""&gt;p&lt;/i&gt;H range&#xD;
from 2 to 7. The experimental data are well represented by Freundlich (&lt;i style=""&gt;n&lt;/i&gt;=0.42, &lt;i style=""&gt;K&lt;sub&gt;f&lt;/sub&gt;&lt;/i&gt;=0.83 L/g, &lt;i style=""&gt;R&lt;sup&gt;2&lt;/sup&gt;&lt;/i&gt;=0.948),&#xD;
Langmuir (&lt;i style=""&gt;R&lt;sub&gt;L&lt;/sub&gt;&lt;/i&gt;=0.566, &lt;i&gt;q&lt;/i&gt;&lt;sub&gt;m&lt;/sub&gt;=&#xD;
3.60 mg/g, &lt;i style=""&gt;R&lt;sup&gt;2&lt;/sup&gt;&lt;/i&gt;=0.991),&#xD;
Redlich-Peterson(&lt;i style=""&gt;R&lt;sup&gt;2&lt;/sup&gt;&lt;/i&gt;=0.98)&#xD;
and Temkin (&lt;i style=""&gt;R&lt;sup&gt;2&lt;/sup&gt;&lt;/i&gt;=0.98, b&lt;sub&gt;T&lt;/sub&gt;&#xD;
=784.52) isotherms, indicating favourable biosorption. The biosorption of Co(II)&#xD;
is described by the pseudo-second order rate equation (&lt;i style=""&gt;K&lt;/i&gt;=0.418 g/mg-min, &lt;i style=""&gt;R&lt;sup&gt;2&lt;/sup&gt;&lt;/i&gt;=0.99)&#xD;
preferably than first order rate equation (&lt;i style=""&gt;R&lt;sup&gt;2&lt;/sup&gt;&lt;/i&gt;=0.89).&#xD;
The biosorption is exothermic, irreversible and spontaneous.
&lt;br/&gt;
&lt;br/&gt;Page(s): 381-390</description>
  </item>
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