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  <channel rdf:about="http://nopr.niscpr.res.in/handle/123456789/20205">
    <title>NOPR Collection:</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/20205</link>
    <description />
    <items>
      <rdf:Seq>
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/20310" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/20309" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/20307" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/20306" />
      </rdf:Seq>
    </items>
    <dc:date>2026-10-10T13:41:03Z</dc:date>
  </channel>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/20310">
    <title>A modified correlation for drop size distribution at different gold concentrations  in chloroauric acid/DBC system</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/20310</link>
    <description>Title: A modified correlation for drop size distribution at different gold concentrations  in chloroauric acid/DBC system
Authors: Javanshir, Sepideh; Abdollahy, Mahmoud; Abolghasemi, Hossein; Sabeti, Hamid
Abstract: The mean diameter of the distribution has been&#xD;
correlated to the mechanical input power, volume phase fraction and &#xD;
gold concentration in &lt;span style="mso-bidi-language:FA" lang="EN-GB"&gt;chloroauric&#xD;
acid/DBC system in a horizontal single stage&#xD;
mixer-settler in the frame of the classical Hinze–Kolmogorov theory. &lt;span style="mso-bidi-language:FA" lang="EN-GB"&gt;Sauter mean diameter (&lt;i&gt;D&lt;sub&gt;32&lt;/sub&gt;&lt;/i&gt;) shows a decrease of 45% &lt;span style="mso-bidi-language:FA" lang="EN-GB"&gt;by increasing impeller speed. In contrast, holdup &lt;span style="mso-bidi-language:&#xD;
FA" lang="EN-GB"&gt;leads to larger drop size. The &lt;i&gt;D&lt;sub&gt;32 &lt;/sub&gt;&lt;/i&gt;increasing&#xD;
rate diminishes about 50% for a system containing 200 ppm gold concentration in&#xD;
aqueous phase with respect to the system with 100 ppm Au. Overall, empirical&#xD;
correlations for drop size at the different conditions are obtained, and a&#xD;
modified correlation for &lt;i&gt;D&lt;/i&gt;&lt;sub&gt;32 &lt;/sub&gt;is presented. The results reveal&#xD;
that &lt;i&gt;D&lt;/i&gt;&lt;sub&gt;32&lt;/sub&gt; depends on the impeller speed with a power low&#xD;
function, and on gold by a linear function as well. The correlation is found to&#xD;
be &#xD;
&lt;i style="mso-bidi-font-style:normal"&gt;D&lt;/i&gt;&lt;sub&gt;&lt;span style="mso-bidi-font-size:9.0pt" lang="EN-GB"&gt;32&lt;/span&gt;&lt;/sub&gt;&lt;span style="mso-bidi-font-size:9.0pt" lang="EN-GB"&gt;/&lt;i style="mso-bidi-font-style:normal"&gt;D&lt;/i&gt;=(–0.709C&lt;sub&gt;Au&lt;/sub&gt;+0.823)(1+2.022ϕ)&lt;span style="mso-bidi-font-size:9.0pt;mso-bidi-font-style:italic" lang="EN-GB"&gt;&lt;i&gt;W&lt;/i&gt;&lt;sub&gt;e&lt;/sub&gt;&lt;sup&gt;–0.865&lt;/sup&gt;&lt;span style="font-size:10.0pt;mso-bidi-font-style:italic" lang="EN-GB"&gt;. The calculated average absolute relative deviation is found to be less&#xD;
than &#xD;
4.5%, showing &lt;span style="mso-bidi-language:FA" lang="EN-GB"&gt;good&#xD;
conformity to experimental data.&#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;
Page(s): 259-264</description>
    <dc:date>2013-07-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/20309">
    <title>Solvent extraction separation of zirconium (IV) with 2-octylaminopyridine  from succinate media—Analysis of real samples</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/20309</link>
    <description>Title: Solvent extraction separation of zirconium (IV) with 2-octylaminopyridine  from succinate media—Analysis of real samples
Authors: Noronha, Leena E; Kamble, Ganesh S; Kolekar, Sanjay S; Anuse, Mansing A
Abstract: A systematic study on liquid-liquid&#xD;
extraction separation of zirconium (IV) from 25 mL 0.02 M sodium succinate&#xD;
solution using 10 mL 0.087 M 2-Octylaminopyridine (2-OAP) as an extractant has&#xD;
been carried out. Quantitative extraction of Zr (IV) is observed at &lt;i style="mso-bidi-font-style:normal"&gt;p&lt;/i&gt;H 3.7 – 5.0 using 0.01 – 0.03 M sodium&#xD;
succinate with 0.087 M 2-OAP in xylene. Zirconium (IV) has been back extracted&#xD;
with 0.5 M HNO&lt;sub&gt;3&lt;/sub&gt; (3×10 mL). The nature of extracted species in&#xD;
organic phase is determined by using conventional slope analysis method. The&#xD;
proposed method is applicable to separate Zr (IV) from associated metals like&#xD;
W(VI), Fe(III), Mo(VI), Y(III), Al(III), V(V), U(VI) and Th(IV) and also in the&#xD;
analysis of Zr (IV) from various synthetic mixtures, real samples of alloy,&#xD;
thin films and nanopowder.
Page(s): 252-258</description>
    <dc:date>2013-07-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/20307">
    <title>Equilibrium uptake and sorption dynamics for the removal of reactive dyes from aqueous solution using activated carbon prepared from &lt;i&gt;E&lt;/i&gt;&lt;i style="mso-bidi-font-style: normal"&gt;uphorbia tirucalli L&lt;/i&gt; wood</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/20307</link>
    <description>Title: Equilibrium uptake and sorption dynamics for the removal of reactive dyes from aqueous solution using activated carbon prepared from &lt;i&gt;E&lt;/i&gt;&lt;i style="mso-bidi-font-style: normal"&gt;uphorbia tirucalli L&lt;/i&gt; wood
Authors: Palanisamy, P N; Agalya, A; Sivakumar, P
Abstract: Activated carbon prepared from &lt;i style="mso-bidi-font-style:normal"&gt;&lt;span style="mso-bidi-font-weight:bold"&gt;Euphorbia&#xD;
tirucalli L &lt;/span&gt;&lt;/i&gt;wood (ETAC) by chemical activation with phosphoric acid&#xD;
has been analysed for the removal of Reactive Red and Reactive Blue dyes from&#xD;
aqueous solutions through batch adsorption technique. Lower solution &lt;i style="mso-bidi-font-style:normal"&gt;p&lt;/i&gt;H favours the adsorption of reactive&#xD;
dyes. The amount of dye adsorbed per unit mass of adsorbent increases with the&#xD;
increase in temperature and initial dye concentration. Freundlich and Langmuir&#xD;
models are used to analyze the equilibrium data at different temperatures. The&#xD;
equilibrium data for the adsorption of both dyes are better described by the&#xD;
Langmuir isotherm model. The adsorption of reactive dyes follows second order&#xD;
kinetics along with &#xD;
intra-particle diffusion model. Thermodynamic parameters such as free energy&#xD;
change, enthalpy change and entropy change for adsorption of reactive dyes show&#xD;
that the adsorption of Reactive Red and Reactive Blue onto ETAC are&#xD;
spontaneous, endothermic and physical adsorption. Activation energy and&#xD;
isosteric heat of adsorption suggests that adsorption of reactive dyes onto&#xD;
ETAC is a physical process.
Page(s): 245-251</description>
    <dc:date>2013-07-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/20306">
    <title>Corrosion inhibition of brass in presence of 1, 4, 5, 6-tetrahydropyrimidine derivatives in chloride solution</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/20306</link>
    <description>Title: Corrosion inhibition of brass in presence of 1, 4, 5, 6-tetrahydropyrimidine derivatives in chloride solution
Authors: Ranjana; Banerjee, Ranu; Nandi, M M
Abstract: The inhibition effects of L (-) aspartic&#xD;
acid (I) and its various derivatives namely N-benzenesulphonyl L (-) aspartic&#xD;
acid (II), α-benzenesulphonamido-β-2-(1, 4, 5, 6-tetrahydropyrimidinyl)&#xD;
propionic acid (III) and 1-benzenesulphonamido-1,&#xD;
2-bis-2(1,4,5,6-tetrahydropyrimidinyl) ethane (IV) against the corrosion of&#xD;
brass in 0.6 M aqueous sodium chloride solution have been studied using&#xD;
potentiodynamic polarization and electrochemical impedance spectroscopy. The&#xD;
inhibition efficiency of these compounds increases in the order I &amp;lt; II &amp;lt;&#xD;
III &amp;lt; IV. The inhibition efficiency of IV with 4 × 10 &lt;sup&gt;-5&lt;/sup&gt; M&#xD;
concentration is the highest which reaches 94.9%. It is observed that the introduction&#xD;
of C&lt;sub&gt;6&lt;/sub&gt;H&lt;sub&gt;5&lt;/sub&gt;SO&lt;sub&gt;2&lt;/sub&gt;- group increases the inhibition&#xD;
efficiency of L (-) aspartic acid by 32.0%. Conversion of one –COOH group to 1,&#xD;
4, 5, 6-tetrahydropyrimidine increases inhibition efficiency by 15.5% and when&#xD;
both the –COOH groups are converted to 1,4,5,6–tetrahydropyrimidine the&#xD;
inhibition efficiency becomes maximum (95%). This is due to higher molecular&#xD;
size, π – electron contribution of the benzene ring, and presence of more&#xD;
active adsorption sites.
Page(s): 237-244</description>
    <dc:date>2013-07-01T00:00:00Z</dc:date>
  </item>
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