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    <title>NOPR Collection:</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/22610</link>
    <description />
    <items>
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        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/22754" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/22753" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/22752" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/22751" />
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    <dc:date>2026-10-10T02:23:26Z</dc:date>
  </channel>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/22754">
    <title>Raoul-Pierre Pictet—The liquefaction of oxygen and achievement of low temperatures</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/22754</link>
    <description>Title: Raoul-Pierre Pictet—The liquefaction of oxygen and achievement of low temperatures
Authors: Wisniak, Jaime
Abstract: To Raoul Pictet (1846-1929) we owe the&#xD;
realization of the liquefaction of oxygen and the study of the effect of low temperatures&#xD;
on physical, chemical, and physiological phenomena. He developed Trouton's law&#xD;
in a theoretical manner, years before Trouton did it by sample tabular&#xD;
means. The priority of oxygen liquefaction was and continues to be a matter of&#xD;
&#xD;
discussion.
Page(s): 326-336</description>
    <dc:date>2003-05-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/22753">
    <title>Selective esterification of triethylene glycol with methacrylic acid using methane sulphonic acid</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/22753</link>
    <description>Title: Selective esterification of triethylene glycol with methacrylic acid using methane sulphonic acid
Authors: Notay, J S; Dahiwale, S M; Bhagade, S S
Abstract: The esterification of tri-ethylene glycol&#xD;
with methacrylic acid under identical conditions of catalyst concentration, for&#xD;
synthesis of tri-ethylene glycol di-methacrylate using sulphuric acid and&#xD;
methane sulphonic acid as catalyst is discussed. The reaction by-products are&#xD;
lesser in case of methane sulphonic acid catalyst, in comparison&#xD;
to sulphuric acid catalyst. Therefore the yield of ester product, tri-ethylene glycol&#xD;
di-methacrylate, achieved during the synthesis is higher with the use of&#xD;
methane sulphonic acid as a catalyst, than on use of sulphuric acid as&#xD;
catalyst. This concludes that methane sulphonic acid has better catalyst&#xD;
selectivity in comparison to sulphuric acid, for the synthesis of tri-ethylene&#xD;
glycol di- methacrylate. Methane sulphonic acid when neutralized is easily bio-degradable&#xD;
which is also desirable from environmental point of view.
Page(s): 324-325</description>
    <dc:date>2003-05-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/22752">
    <title>Thermal analysis of tri-ethylene glycol di-methacrylate</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/22752</link>
    <description>Title: Thermal analysis of tri-ethylene glycol di-methacrylate
Authors: Notay, J S; Dahiwale, S M; Pradhan, S D
Abstract: Thermal characterization of tri-ethylene&#xD;
glycol dimethacrylate was carried out in view of its vast applications. The&#xD;
main objective of this paper is to investigate the thermal behaviour of the&#xD;
impurities present in the compound triethylene glycol di-methacrylate and its&#xD;
effects during applications of the compound. Thermal characterisation was carried&#xD;
out under two different experimental conditions. One at low heat flux rate of&#xD;
10°C/min, and another at higher heat flux rate of 100°C/min. At low heat flux&#xD;
rate, the ethers present as impurities in the compound tri-ethylene glycol&#xD;
dimethacrylate are stable below the temperature of 150°C. This is desirable&#xD;
for applications in anaerobic adhesive and optical articles where exposure to&#xD;
temperature beyond 150°C is not required. At higher heating rate of 100°C/min,&#xD;
the endothermic decomposition of the impurities as ethers present in the&#xD;
compound tri-ethylene glycol di-methacrylate is observed, and the same is desired&#xD;
from the application point of view of using tri-ethylene glycol di-methacrylate&#xD;
as a moderant in single base propellants.&#xD;
&#xD;
 
Page(s): 321-323</description>
    <dc:date>2003-05-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/22751">
    <title>Mass transfer analysis of the extraction of Nickel(II) by emulsion liquid membrane</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/22751</link>
    <description>Title: Mass transfer analysis of the extraction of Nickel(II) by emulsion liquid membrane
Authors: Chakraborty, Mousumi; Bhattacharya, Chiranjib; Datta, Siddhartha
Abstract: A mathematical model for batch extraction&#xD;
of Nickei(II) with emulsion liquid membrane (ELM) from a dilute sulphate&#xD;
solution and from industrial wastewater, using di-(2-ethylhexyl) phosphoric&#xD;
acid (D2EHPA) as extractant and hydrochloric acid as stripping agent is&#xD;
reported. The model considers a reaction front within the emulsion globule and&#xD;
assumes an instantaneous and irreversible reaction between the solute and the&#xD;
internal reagent at the&#xD;
&#xD;
membrane internal droplet interface.&#xD;
Batch experiments are performed for separation of Nickel(II) from aqueous sulphate&#xD;
solution of initial concentration in the range of 100-75 mg/L. The influence of&#xD;
Nickei(II) concentration on the distribution coefficient at pH 3.5 is co-related&#xD;
by a semiempirical model, which has been used for simulation of the extraction&#xD;
process. The simulated curves are found to be in good agreement with the experimental&#xD;
data.
Page(s): 311-320</description>
    <dc:date>2003-05-01T00:00:00Z</dc:date>
  </item>
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