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    <title>NOPR Collection:</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/26138</link>
    <description />
    <pubDate>Sat, 10 Oct 2026 21:26:28 GMT</pubDate>
    <dc:date>2026-10-10T21:26:28Z</dc:date>
    <item>
      <title>Synthesis of polymeric chelating ligands from sago starch for metal removal  from electroplating wastewater</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/26254</link>
      <description>Title: Synthesis of polymeric chelating ligands from sago starch for metal removal  from electroplating wastewater
Authors: Rahman, Md Lutfor; Yusoff, Mashitah Mohd; Malek, Muhammad Nor Fazli Abd; Samah, Nurlin Abu
Abstract: Polymeric chelating ligands containing hydroxamic acid and amidoxime&#xD;
ligands have been synthesized from poly(methyl acrylate-co-acrylonitrile)&#xD;
grafted sago starch. Batch adsorption has been performed to identify the&#xD;
binding property of metal ions. &lt;span style="mso-ansi-language:&#xD;
EN-US;mso-bidi-language:BN" lang="EN-US"&gt;Maximum sorption capacity of copper &lt;span style="mso-ansi-language:EN-US" lang="EN-US"&gt;is found to be 2.80 mmol g&lt;sup&gt;-1&lt;/sup&gt;,&#xD;
however other transition metals has good sorption capacity with this ligands.&#xD;
The rate of exchange of some metals is found to be fast, i.e. &lt;i style="mso-bidi-font-style:normal"&gt;t&lt;/i&gt;&lt;sub&gt;½&lt;/sub&gt; &lt;img src='/image/spc_char/wave.gif' border=0&gt; 6 min (average). Three types of wastewater containing chromium, zinc, nickel, copper,&#xD;
and iron have been used in this study. The metal recovery is found to be high,&#xD;
and more than 99% of the metals could be removed from the metal plating&#xD;
wastewater. Polymeric chelating ligands could be used to remove the metals from&#xD;
wastewater.&#xD;
&#xD;
&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;
Page(s): 30-37</description>
      <pubDate>Wed, 01 Jan 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/26254</guid>
      <dc:date>2014-01-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Evaluation of polymer-agglomerated granular tri-calcium phosphate for fluoride removal from drinking water</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/26253</link>
      <description>Title: Evaluation of polymer-agglomerated granular tri-calcium phosphate for fluoride removal from drinking water
Authors: Sivasankari, C; Arulanantham, A
Abstract: &lt;span style="mso-bidi-font-weight:bold" lang="EN-GB"&gt;The powder&#xD;
and granular forms of tri-calcium phosphate have been used as adsorbents in&#xD;
batch studies for removal of fluoride from aqueous synthetic fluoride&#xD;
solutions. The effects of different operational parameters like &lt;i style="mso-bidi-font-style:normal"&gt;p&lt;/i&gt;H, adsorbent dose, and contact time&#xD;
have been studied for their optimization. Results show that the fluoride&#xD;
removal is maximum and nearly constant in the &lt;i style="mso-bidi-font-style:&#xD;
normal"&gt;p&lt;/i&gt;H range 3.0-8.0. The efficiency of fluoride removal increases with&#xD;
the increase in adsorbent dose and contact time. Surface morphology of the&#xD;
adsorbent has been examined with the scanning electron microscope. Experimental&#xD;
equilibrium adsorption data obtained is found to be fitted well with both&#xD;
Langmuir and Freundlich isotherm models. Adsorption kinetic study reveals that&#xD;
the adsorption process follows pseudo second – order kinetics. Column&#xD;
experiments are performed using granular tri-calcium phosphate (GTCP) to find&#xD;
out the optimum flow rate, bed height and the effect of co-existing anions in&#xD;
water. The optimum fluoride removal capacity in column study is found to be&#xD;
2.1005 mg of fluoride per gram of GTCP. Regeneration of the adsorbent for&#xD;
repeated use has also been studied in column operation and it is established&#xD;
that complete regeneration could be achieved with 0.5% aluminium sulphate&#xD;
solution for 8 cycles without loss of efficiency. &#xD;
&#xD;
&lt;/span&gt;
Page(s): 70-77</description>
      <pubDate>Wed, 01 Jan 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/26253</guid>
      <dc:date>2014-01-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Self sustained autogenous dissolution of medium grade manganese ore of Gujarat in NH&lt;sub&gt;3&lt;/sub&gt;OHCl-H&lt;sub&gt;2&lt;/sub&gt;SO&lt;sub&gt;4&lt;/sub&gt;-H&lt;sub&gt;2&lt;/sub&gt;O medium</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/26252</link>
      <description>Title: Self sustained autogenous dissolution of medium grade manganese ore of Gujarat in NH&lt;sub&gt;3&lt;/sub&gt;OHCl-H&lt;sub&gt;2&lt;/sub&gt;SO&lt;sub&gt;4&lt;/sub&gt;-H&lt;sub&gt;2&lt;/sub&gt;O medium
Authors: Hariprasad, D; Mohapatra, M; Rao, K Srinivasa; Anand, S
Abstract: &lt;span style="mso-fareast-language:EN-IN;&#xD;
mso-bidi-font-style:italic" lang="EN-GB"&gt;Leaching studies have been&#xD;
carried&lt;span style="mso-fareast-language:EN-IN;mso-bidi-font-style:&#xD;
italic" lang="EN-GB"&gt; for dissolution of manganese from medium grade manganese ore in hydroxyl ammine hydrochloride-sulphuric acid medium. Due to&#xD;
exothermic nature of reaction no external heat is required for quantitative&#xD;
extraction of manganese confirming the self sustained autogenous nature of&#xD;
leaching process. Initially, the effects of individual parameters &lt;span style="mso-bidi-font-weight:bold;mso-bidi-font-style:italic"&gt;including time,&#xD;
sulphuric &lt;span style="mso-bidi-font-weight:bold"&gt;acid concentration,&#xD;
amount of reductant, pulp density, and particle size have been studied. One&#xD;
parameter has been changed at a time while keeping the other parameters&#xD;
constant. Per cent manganese extraction is found to be dependent on acid&#xD;
concentration and amount of reductant. Within 20 min, manganese could be&#xD;
quantitatively dissolved. A comparison of FTIR spectra of synthetic solution&#xD;
with actual leach solution indicates the formation of ClO&lt;sub&gt;4&lt;/sub&gt;&lt;sup&gt;-&lt;/sup&gt;&#xD;
ions during leaching. The XRD pattern of the residue shows only quartz as the&#xD;
crystalline phase. Response surface methodology is&lt;span style="mso-bidi-font-weight:bold"&gt; adopted applying a central composite&#xD;
design for 2&lt;sup&gt;4&lt;/sup&gt; factorial set of experiments.&lt;span style="mso-bidi-font-weight:&#xD;
bold"&gt; &#xD;
A statistical analysis is done to evaluate interactive effects.&lt;span style="mso-bidi-font-weight:bold"&gt; Using the model, optimised parameters&#xD;
&lt;span style="mso-bidi-font-weight:bold"&gt;in the range of pulp density 25 - 35 %&#xD;
wt /v, acid concentration 6.5-7.5% v/v, amount of reductant 15-16 g and time 10 - 30 min have&#xD;
been considered for maximum desirability. The experimental data is found&#xD;
to be fitted well with the predicted ones.&lt;span style="mso-bidi-font-weight:&#xD;
bold"&gt;&#xD;
&#xD;
&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;
Page(s): 63-69</description>
      <pubDate>Wed, 01 Jan 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/26252</guid>
      <dc:date>2014-01-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Kinetic modelling of Fe&lt;sup&gt;3+&lt;/sup&gt; ion uptake by zeolite from water</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/26251</link>
      <description>Title: Kinetic modelling of Fe&lt;sup&gt;3+&lt;/sup&gt; ion uptake by zeolite from water
Authors: Ćurković, L; Bolanča, T; Šiljeg, M; Foglar, L
Abstract: The ability of the natural clinoptilolite&#xD;
(Cp), and its Na–enriched form (Na–Cp) to remove&#xD;
iron ions from acid aqueous solutions has been investigated in the batch system&#xD;
at the initial concentration of 100 mg Fe&lt;sup&gt;3+&lt;/sup&gt;/L, &lt;i style="mso-bidi-font-style:&#xD;
normal"&gt;p&lt;/i&gt;H value of 1.90, and the equilibration time of 30–300 min. In&#xD;
order to establish the Fe&lt;sup&gt;3+&lt;/sup&gt; uptake behaviour, the rate controlling&#xD;
step of the process and to determine the coefficients, the ion exchange&#xD;
kinetics have been investigated and the different models usually applied are&#xD;
used for description of adsorption kinetics. The Fe&lt;sup&gt;3+&lt;/sup&gt; uptake by Cp&#xD;
and Na-Cp is evaluated based on the first–order kinetics, modified Freundlich&#xD;
and Elovich models, parabolic diffusion and heterogeneous diffusion models.&#xD;
Developed models can successfully describe the ion exchange processes between&#xD;
Fe&lt;sup&gt;3+&lt;/sup&gt;:Cp and Fe&lt;sup&gt;3+&lt;/sup&gt;:Na–Cp. In addition, the results show&#xD;
that the natural Croatian clinoptilolite enables efficient removal of iron from&#xD;
water.
Page(s): 56-62</description>
      <pubDate>Wed, 01 Jan 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/26251</guid>
      <dc:date>2014-01-01T00:00:00Z</dc:date>
    </item>
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