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    <title>NOPR Collection:</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/30965</link>
    <description />
    <items>
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        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/31019" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/31018" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/31017" />
        <rdf:li rdf:resource="http://nopr.niscpr.res.in/handle/123456789/31016" />
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    <dc:date>2026-10-10T07:53:32Z</dc:date>
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  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/31019">
    <title>Modification of polysulphone with cellulose acetate and application as membranes</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/31019</link>
    <description>Title: Modification of polysulphone with cellulose acetate and application as membranes
Authors: Sivakumar, M; Mohan, D; Mohan, V; Lakshmanan, C M
Abstract: &lt;span style="font-size:11.0pt;font-family:" calibri","sans-serif";="" mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"times="" new="" roman";="" mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;color:black;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"=""&gt;Ultrafiltration&#xD;
gains significance when certain chemical species present in low concentration&#xD;
have to be selectively removed from a multicomponent mixture containing certain&#xD;
heavy metal ions. Polysulphone is considered as the most promising candidate as&#xD;
ultrafiltration membrane. The use of polysulphonein aqueous separation is&#xD;
restricted due to its high hydrophobic nature. For aqueous separation, the&#xD;
blending of polysulphone with cellulose diacetate in solution medium using&#xD;
polar solvents was attempted. The effects of polymer and additive concentration&#xD;
have been studied. The modified membranes were subjected to pure water&#xD;
permeability and were applied for separation of metal ion in aqueous medium and&#xD;
the results are discussed.&lt;/span&gt;
Page(s): 184-186</description>
    <dc:date>1996-05-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/31018">
    <title>Mathematical modelling and computer simulation of molecular transport of benzene into tetrafluoroethylene/propylene copolymer membranes</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/31018</link>
    <description>Title: Mathematical modelling and computer simulation of molecular transport of benzene into tetrafluoroethylene/propylene copolymer membranes
Authors: Aminabhavi, Tejraj M; Phayde, Hemant T S
Abstract: &lt;span style="font-size:11.0pt;font-family:" calibri","sans-serif";="" mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"times="" new="" roman";="" mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;color:black;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"=""&gt;Kinetic&#xD;
curves for sorption/desorption cycles have been generated for&#xD;
tetrafluoroethylene/propylene copolymer membranes at 25, 40, 55 and 70&lt;sup&gt;0&lt;/sup&gt;C&#xD;
by a gravimetric method. Diffusion coefficients have been obtained from the&#xD;
mathematical relations derived from Fick's relation. Numerical scheme based on&#xD;
the finite difference method has been used to describe the sorption/desorption processes.&#xD;
Theoretical kinetic curves have been compared well with the experimental values&#xD;
before 55% equilibrium saturation.&lt;/span&gt;
Page(s): 178-183</description>
    <dc:date>1996-05-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/31017">
    <title>Use of aromatic polyamide membranes in desalination</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/31017</link>
    <description>Title: Use of aromatic polyamide membranes in desalination
Authors: Biware, M V; Ghatge, N D
Abstract: &lt;span style="font-size:11.0pt;font-family:" calibri","sans-serif";="" mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"times="" new="" roman";="" mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;color:black;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"=""&gt;Piperazine&#xD;
containing polymers, having no 'H' atom at amide nitrogen have been prepared&#xD;
from diaminobenzanilides and diacid chlorides by low temperature&#xD;
polycondensation method. These polymers have been characterised by inherent&#xD;
viscosity, percent moisture regain, solubility, IR and thermal analysis. Amount&#xD;
of chlorine absorbed by the polyamides has been calculated by titrating polymer&#xD;
suspension with sodium thiosulphate. Membranes were cast from the polymer&#xD;
solution in dimethyl acetamide containing lithium chloride as an additive.&#xD;
These membranes' were studied for reverse osmosis (RO) performance in salt&#xD;
water with and without chlorine containing medium.&lt;/span&gt;
Page(s): 173-177</description>
    <dc:date>1996-05-01T00:00:00Z</dc:date>
  </item>
  <item rdf:about="http://nopr.niscpr.res.in/handle/123456789/31016">
    <title>An electro-membrane process for dibromopropanol epoxidation</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/31016</link>
    <description>Title: An electro-membrane process for dibromopropanol epoxidation
Authors: Manaf, A; Audinos, R
Abstract: &lt;span style="font-size:11.0pt;font-family:" calibri","sans-serif";="" mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"times="" new="" roman";="" mso-hansi-theme-font:minor-latin;mso-bidi-font-family:arial;color:black;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"=""&gt;In&#xD;
this paper, an electro-membrane process has been described which allows to&#xD;
perform cyclodehydrohalogenation of dibromopropanols into epibromhydrin at room&#xD;
temperature. Epoxidation occurs in the stack fitted with ion exchange membranes&#xD;
when a constant direct current is applied on end electrodes. Hydroxyl ions are&#xD;
continuously fed into the reacting cell as bromide ions arelextracted, and it&#xD;
is not necessary with such a membrane reactor, to use a down-stream&#xD;
purification of the epibromhydrin produced. The mass yield in the, reacting&#xD;
cell was 70 ± 5%, due to diffusion of reactants and/or products through the&#xD;
membranes used.&lt;/span&gt;
Page(s): 168-172</description>
    <dc:date>1996-05-01T00:00:00Z</dc:date>
  </item>
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