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  <title>NOPR Collection:</title>
  <link rel="alternate" href="http://nopr.niscpr.res.in/handle/123456789/8566" />
  <subtitle />
  <id>http://nopr.niscpr.res.in/handle/123456789/8566</id>
  <updated>2026-10-13T05:09:30Z</updated>
  <dc:date>2026-10-13T05:09:30Z</dc:date>
  <entry>
    <title>Inhibition of corrosion of mild steel in hydrochloric acid by &lt;i style=""&gt;N&lt;/i&gt;-cyclohexyl-&lt;i style=""&gt;N&lt;/i&gt;'- phenyl thiourea</title>
    <link rel="alternate" href="http://nopr.niscpr.res.in/handle/123456789/8667" />
    <author>
      <name>Shetty, S Divakara</name>
    </author>
    <author>
      <name>Shetty, Prakash</name>
    </author>
    <author>
      <name>Nayak, H V Sudhaker</name>
    </author>
    <id>http://nopr.niscpr.res.in/handle/123456789/8667</id>
    <updated>2010-05-08T16:30:27Z</updated>
    <published>2005-07-01T00:00:00Z</published>
    <summary type="text">Title: Inhibition of corrosion of mild steel in hydrochloric acid by &lt;i style=""&gt;N&lt;/i&gt;-cyclohexyl-&lt;i style=""&gt;N&lt;/i&gt;'- phenyl thiourea
Authors: Shetty, S Divakara; Shetty, Prakash; Nayak, H V Sudhaker
Abstract: &lt;smarttagtype namespaceuri="urn:schemas-microsoft-com:office:smarttags" name="place"&gt;&#xD;
&#xD;
&#xD;
&#xD;
The inhibition&#xD;
of corrosion of mild steel in 0.01-0.1 N HCl&#xD;
solutions by &lt;i style=""&gt;N&lt;/i&gt;-cyclohexyl-&lt;i style=""&gt;N&lt;/i&gt;'-phenyl thiourea (CPTU) has&#xD;
been studied using potentiodynamic polarization technique. Results obtained&#xD;
reveal that CPTU performs excellently as anodic inhibitor for mild steel in HCl&#xD;
solution. The inhibitor functions through adsorption following Temkins’&#xD;
adsorption isotherm. The influence of parameters like temperature, hydrochloric&#xD;
acid concentration and inhibitor concentration on the corrosion of mild steel&#xD;
has also been studied. &#xD;
&#xD;
&lt;/smarttagtype&gt;
Page(s): 462-465</summary>
    <dc:date>2005-07-01T00:00:00Z</dc:date>
  </entry>
  <entry>
    <title>Micellar–enhanced ultrafiltration of chromate [Cr(VI)] ion from aqueous streams by using cationic surfactant</title>
    <link rel="alternate" href="http://nopr.niscpr.res.in/handle/123456789/8666" />
    <author>
      <name>Kamble, S B</name>
    </author>
    <author>
      <name>Marathe, K V</name>
    </author>
    <id>http://nopr.niscpr.res.in/handle/123456789/8666</id>
    <updated>2010-05-03T16:30:48Z</updated>
    <published>2005-07-01T00:00:00Z</published>
    <summary type="text">Title: Micellar–enhanced ultrafiltration of chromate [Cr(VI)] ion from aqueous streams by using cationic surfactant
Authors: Kamble, S B; Marathe, K V
Abstract: &lt;smarttagtype namespaceuri="urn:schemas-microsoft-com:office:smarttags" name="country-region"&gt;&lt;smarttagtype namespaceuri="urn:schemas-microsoft-com:office:smarttags" name="place"&gt;&#xD;
&#xD;
&#xD;
&#xD;
Hexavalent chromium&#xD;
[Cr(VI)] in industrial effluent is one of the most serious environmental&#xD;
problems in India&#xD;
and also in other countries. Micellar-Enhanced Ultrafiltration (MEUF) of the&#xD;
chromate anions from aqueous solutions has been studied at room temperature&#xD;
(28±2°C) using cationic surfactants,&#xD;
cetyltrimethylammonium bromide (CTAB) and cetylpyridinium chloride (CPC),&#xD;
micelles of which adsorb the chromate ions by electrostatic interactions. The&#xD;
solution is processed by ultrafiltration, using a membrane with a pore size&#xD;
small enough to block the passage of the micelles and the adsorbed ions. The&#xD;
process is highly efficient in removing the chromate ions. In the absence of other&#xD;
electrolytes, chromate ion rejection up to 99% was observed at optimal&#xD;
conditions of pH, pressure, temperature, feed chromate and surfactant&#xD;
concentrations. The presence of added NaCl reduces the chromate rejection, but&#xD;
it was still considerable (up to 82%), even in the presence of 100 mM NaCl. The&#xD;
rejection rate of chromate was found to be highly dependent on the pH of the&#xD;
feed solution. The solute rejection is also affected by anion charge density,&#xD;
and interaction of fixed membrane charge sites with ionic solutes.&#xD;
&#xD;
&lt;/smarttagtype&gt;&lt;/smarttagtype&gt;
Page(s): 393-400</summary>
    <dc:date>2005-07-01T00:00:00Z</dc:date>
  </entry>
  <entry>
    <title>Pinacol-Pinacolone rearrangement over solids supported metal ion catalysts</title>
    <link rel="alternate" href="http://nopr.niscpr.res.in/handle/123456789/8665" />
    <author>
      <name>Shamshuddin, S Z Mohamed</name>
    </author>
    <author>
      <name>Kuriakose, George</name>
    </author>
    <author>
      <name>Nagaraju, N</name>
    </author>
    <id>http://nopr.niscpr.res.in/handle/123456789/8665</id>
    <updated>2010-05-04T16:30:46Z</updated>
    <published>2005-07-01T00:00:00Z</published>
    <summary type="text">Title: Pinacol-Pinacolone rearrangement over solids supported metal ion catalysts
Authors: Shamshuddin, S Z Mohamed; Kuriakose, George; Nagaraju, N
Abstract: Catalytic activity of hydrated Al&lt;sub&gt;2&lt;/sub&gt;O&lt;sub&gt;3&lt;/sub&gt;,&#xD;
SiO&lt;sub&gt;2&lt;/sub&gt;, ZrO&lt;sub&gt;2&lt;/sub&gt;,&lt;sub&gt; &lt;/sub&gt;AlPO&lt;sub&gt;4&lt;/sub&gt;, zeolite-HY and&#xD;
Fe(III) ions supported on these solids has been evaluated in pinacol-pinacolone&#xD;
rearrangement (2,3-dimethyl-2,3-butanediol to 3,3-dimethyl-2-butanone). The&#xD;
effect of method of preparation of catalysts on their catalytic activity has&#xD;
been evaluated. Studies on catalytic activity have been performed in vapour&#xD;
phase at different reaction temperatures. Pinacolone and&#xD;
2,3-dimethyl-1,3-butadiene were formed as the major products. The percentage&#xD;
conversion of pinacol and the selectivity of the products have been found to be&#xD;
influenced by the reaction temperature, the nature of the support, the metal&#xD;
ion present on the support and the method of preparation of supported&#xD;
catalysts. Al&lt;sub&gt;2&lt;/sub&gt;O&lt;sub&gt;3&lt;/sub&gt; and AlPO&lt;sub&gt;4&lt;/sub&gt; containing 5% Fe&#xD;
ions on their surface are found to convert pinacol to pinacolone to an extent&#xD;
of 88% with a selectivity of 83% for ketone at 200 °C with 10 mL/h flow rate of the reactant. A comparative study of the&#xD;
catalytic activity of the materials containing 5% Fe ions on Al&lt;sub&gt;2&lt;/sub&gt;O&lt;sub&gt;3&lt;/sub&gt;&#xD;
and those containing same percentage of Ni or Co ions in the chosen reaction at&#xD;
200 °C, revealed a good correlation between&#xD;
the redox potential of the metal ions and their selective catalytic activity in&#xD;
the formation of pinacolone.
Page(s): 447-454</summary>
    <dc:date>2005-07-01T00:00:00Z</dc:date>
  </entry>
  <entry>
    <title>Removal and recovery of lead from aqueous solution using  supported liquid membrane</title>
    <link rel="alternate" href="http://nopr.niscpr.res.in/handle/123456789/8664" />
    <author>
      <name>Anupama, R</name>
    </author>
    <author>
      <name>Palanivelu, K</name>
    </author>
    <id>http://nopr.niscpr.res.in/handle/123456789/8664</id>
    <updated>2010-05-07T16:30:31Z</updated>
    <published>2005-07-01T00:00:00Z</published>
    <summary type="text">Title: Removal and recovery of lead from aqueous solution using  supported liquid membrane
Authors: Anupama, R; Palanivelu, K
Abstract: A laboratory study was conducted to remove and&#xD;
recover lead from aqueous solution using supported liquid membrane (SLM)&#xD;
process. Preliminary solvent extraction studies, on lead revealed the iodo&#xD;
system with tributyl phosphate (TBP) as liquid membrane and sodium hydroxide as&#xD;
strippant to be an efficient one. Using synthetic lead(II) solution, the&#xD;
process parameters like feed side pH, strippant concentration, KI concentration&#xD;
and stirring speed were optimized. The initial lead concentration of 25 mg/L gave&#xD;
satisfactory result with complete removal and recovery in 4 h of operation with&#xD;
a permeability coefficient of 1.146 × 10&lt;sup&gt;-5&lt;/sup&gt; m/s.
Page(s): 436-440</summary>
    <dc:date>2005-07-01T00:00:00Z</dc:date>
  </entry>
</feed>

