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    <title>NOPR Collection:</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/32093</link>
    <description />
    <pubDate>Sat, 10 Oct 2026 18:19:41 GMT</pubDate>
    <dc:date>2026-10-10T18:19:41Z</dc:date>
    <item>
      <title>Comparative study on the removal of copper (II) and nickel (II) from  aqueous soluion using cellulose extracted from sisal fiber and cellulose  grafted acrylonitrile copolymer</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/32139</link>
      <description>Title: Comparative study on the removal of copper (II) and nickel (II) from  aqueous soluion using cellulose extracted from sisal fiber and cellulose  grafted acrylonitrile copolymer
Authors: Hajeeth, T; Gomathi, T; Sudha, P N
Abstract: &lt;span style="font-size:11.0pt;mso-bidi-font-size:&#xD;
10.0pt;font-family:" times="" new="" roman","serif";mso-fareast-font-family:gulliverrm;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"="" lang="EN-US"&gt;Batch&#xD;
adsorption studies have been carried out to&lt;span style="font-size:11.0pt;mso-bidi-font-size:10.0pt;font-family:" times="" new="" roman","serif";="" mso-fareast-font-family:"times="" roman";mso-ansi-language:en-us;mso-fareast-language:="" en-us;mso-bidi-language:ar-sa"="" lang="EN-US"&gt; &lt;span style="font-size:11.0pt;&#xD;
mso-bidi-font-size:10.0pt;font-family:" times="" new="" roman","serif";mso-fareast-font-family:="" gulliverrm;mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:="" ar-sa"="" lang="EN-US"&gt;remove &lt;span style="font-size:11.0pt;mso-bidi-font-size:&#xD;
10.0pt;font-family:" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:ar-sa"="" lang="EN-US"&gt;Cu&#xD;
(II) and Ni (II) ion from aqueous solution using cellulose extracted from sisal&#xD;
fiber and cellulose-g-acrylonitrile copolymer by steam explosion method.&lt;span style="mso-bidi-font-style:italic"&gt; The effect of &lt;i style="mso-bidi-font-style:&#xD;
normal"&gt;p&lt;/i&gt;&lt;span style="mso-bidi-font-style:italic"&gt;H, contact time and&#xD;
amount of adsorbent dose have also been investigated for both cellulose&#xD;
extracted from sisal fiber and cellulose-g-acrylonitrile copolymer&lt;span style="mso-bidi-font-style:italic"&gt; . From the observed results, it is&#xD;
evident that the adsorption of metal ions increases with the increase in&#xD;
contact time and adsorbent dosage. The optimum &lt;i&gt;p&lt;/i&gt;H is found to be 5.0 for&#xD;
the removal of copper (II) and nickel (II) for both the extracted cellulose and&#xD;
cellulose-g-acrylonitrile copolymer.&lt;span style="mso-bidi-font-style:italic"&gt;&#xD;
The adsorption kinetics of cellulose and cellulose-g-acrylonitrile is found to&#xD;
follow pseudo-second-order kinetic model. The experimental data are fitted to&#xD;
Langmuir adsorption isotherms for both cellulose extracted from sisal&#xD;
fiber and cellulose-g-acrylonitrile copolymer.&lt;span style="mso-bidi-font-style:&#xD;
italic"&gt; From the results it is concluded that the cellulose graft acrylonitrile&#xD;
copolymer is found to be efficient adsorbent for the removal of heavy metals&#xD;
from aqeous solutions.&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): 328-337</description>
      <pubDate>Mon, 01 Sep 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/32139</guid>
      <dc:date>2014-09-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Effect of alkali treatment process parameters on semi refined carrageenan functional groups</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/32138</link>
      <description>Title: Effect of alkali treatment process parameters on semi refined carrageenan functional groups
Authors: Anisuzzaman, S M; Bono, Awang; Krishnaiah, Duduku; Ariffin, Buhri; Lee, Ricky
Abstract: &lt;span style="font-size:11.0pt;font-family:&#xD;
" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";mso-bidi-font-family:="" mangal;mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:="" hi"="" lang="EN-US"&gt;Semi refined carrageenan (SRC) has been produced by alkali treatment from&#xD;
the seaweed &lt;span style="font-size:11.0pt;font-family:" times="" new="" roman","serif";="" mso-fareast-font-family:"times="" roman";mso-bidi-font-family:mangal;="" mso-ansi-language:en-gb;mso-fareast-language:en-us;mso-bidi-language:hi"="" lang="EN-GB"&gt;Kappaphytus&lt;i style="mso-bidi-font-style:normal"&gt;&lt;span style="font-size:11.0pt;&#xD;
font-family:" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";="" mso-bidi-font-family:mangal;mso-ansi-language:en-us;mso-fareast-language:en-us;="" mso-bidi-language:hi"="" lang="EN-US"&gt; alvarezii. &lt;/span&gt;&lt;/i&gt;&lt;span style="font-size:&#xD;
11.0pt;font-family:" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";="" mso-bidi-font-family:mangal;mso-ansi-language:en-us;mso-fareast-language:en-us;="" mso-bidi-language:hi"="" lang="EN-US"&gt;The effect of two alkali treatment process parameters;&#xD;
variation of potassium hydroxide (KOH) concentration and cooking temperature on&#xD;
SRC functional group has been investigated. The KOH concentration and&#xD;
temperature are in the range of 6-9%w/w and 60-80&lt;span style="font-size:11.0pt;font-family:Symbol;mso-ascii-font-family:" times="" new="" roman";="" mso-fareast-font-family:"times="" roman";mso-hansi-font-family:"times="" mso-bidi-font-family:mangal;mso-ansi-language:en-us;mso-fareast-language:en-us;="" mso-bidi-language:hi;mso-char-type:symbol;mso-symbol-font-family:symbol"="" lang="EN-US"&gt;°&lt;span style="font-size:11.0pt;font-family:" times="" new="" roman","serif";="" mso-fareast-font-family:"times="" roman";mso-bidi-font-family:mangal;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:hi"="" lang="EN-US"&gt;C&#xD;
respectively at 60 min. The SRC powder is prepared using spray drying technique&#xD;
of SRC solution. The total absorption or compositions functional groups of SRC&#xD;
powder have been determined by &lt;span style="font-size:11.0pt;&#xD;
font-family:" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";="" mso-bidi-font-family:mangal;mso-ansi-language:en-gb;mso-fareast-language:en-us;="" mso-bidi-language:hi"="" lang="EN-GB"&gt;Fourier transform infrared spectroscopy (&lt;span style="font-size:11.0pt;font-family:" times="" new="" roman","serif";="" mso-fareast-font-family:"times="" roman";mso-bidi-font-family:mangal;="" mso-ansi-language:en-us;mso-fareast-language:en-us;mso-bidi-language:hi"="" lang="EN-US"&gt;FTIR).&#xD;
The analysis of experimental data shows that the investigated functional group&#xD;
composition of SRC produced is very much affected by KOH concentration. The&#xD;
predicted values of functional groups of sulphation, 3,6-anhydrous-G-galactose&#xD;
and D-galactose-4-sulphate are 1233.93, 928.41, 848.12 cm&lt;sup&gt;-1&lt;/sup&gt;&#xD;
respectively.&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;
Page(s): 386-391</description>
      <pubDate>Mon, 01 Sep 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/32138</guid>
      <dc:date>2014-09-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Removal of molybdenum (VI) from effluent waste water streams by cross  flow micellar enhanced ultrafiltration (MEUF) using anionic, non-ionic  and mixed surfactants</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/32137</link>
      <description>Title: Removal of molybdenum (VI) from effluent waste water streams by cross  flow micellar enhanced ultrafiltration (MEUF) using anionic, non-ionic  and mixed surfactants
Authors: Yobilishetty, Swathi M; Marathe, K V
Abstract: &lt;span style="font-size:9.0pt;font-family:&#xD;
" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";mso-bidi-font-family:="" mangal;mso-ansi-language:en-gb;mso-fareast-language:en-us;mso-bidi-language:="" hi"="" lang="EN-GB"&gt;Micellar Enhanced Ultrafiltration (MEUF) has been used to remove dissolved&#xD;
molybdenum efficiently from the waste streams by using two surfactants: sodium&#xD;
dodecyl sulfate (SDS) and Tween 20 in a lab-scale membrane system. Effect of&#xD;
feed flow rate, time, molar ratio of surfactant to metal (S/M ratio), feed &lt;i&gt;p&lt;/i&gt;H&#xD;
and feed molybdenum concentration on %rejection of molybdenum has been studied.&#xD;
Effect of non-ionic (Tween 20) and mixed surfactant (SDS + Tween 20) on&#xD;
%rejection of molybdenum is also studied. Molybdenum is removed by 90.3% at&#xD;
optimized parameters (feed flow rate, time, S/M ratio, &lt;i&gt;p&lt;/i&gt;H, feed&#xD;
molybdenum concentration, concentration of SDS) and non-ionic and mixed&#xD;
surfactants removed molybdenum by 92 and 90.4% respectively. Distribution&#xD;
coefficient, loading of micelles and micellar binding constants have been&#xD;
calculated for both the anionic surfactant and mixed surfactant from&#xD;
experimental results. Gel layer formation is found to be negligible since all&#xD;
experiments have been carried out at low range of pollutants.&lt;/span&gt;
Page(s): 321-327</description>
      <pubDate>Mon, 01 Sep 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/32137</guid>
      <dc:date>2014-09-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>&lt;span style="font-size:11.0pt;font-family: "Times New Roman","serif";mso-fareast-font-family:"Times New Roman";mso-bidi-font-family: Mangal;text-transform:uppercase;mso-ansi-language:EN-GB;mso-fareast-language: EN-US;mso-bidi-language:HI" lang="EN-GB"&gt;A &lt;span style="font-size:11.0pt; font-family:"Times New Roman","serif";mso-fareast-font-family:"Times New Roman"; mso-bidi-font-family:Mangal;mso-ansi-language:EN-GB;mso-fareast-language:EN-US; mso-bidi-language:HI" lang="EN-GB"&gt;low cost adsorbent prepared from &lt;i&gt;Curcuma angustifolia&lt;/i&gt; scales for removal of Basic violet 14 from aqueous solution&lt;/span&gt;&lt;/span&gt;</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/32136</link>
      <description>Title: &lt;span style="font-size:11.0pt;font-family: "Times New Roman","serif";mso-fareast-font-family:"Times New Roman";mso-bidi-font-family: Mangal;text-transform:uppercase;mso-ansi-language:EN-GB;mso-fareast-language: EN-US;mso-bidi-language:HI" lang="EN-GB"&gt;A &lt;span style="font-size:11.0pt; font-family:"Times New Roman","serif";mso-fareast-font-family:"Times New Roman"; mso-bidi-font-family:Mangal;mso-ansi-language:EN-GB;mso-fareast-language:EN-US; mso-bidi-language:HI" lang="EN-GB"&gt;low cost adsorbent prepared from &lt;i&gt;Curcuma angustifolia&lt;/i&gt; scales for removal of Basic violet 14 from aqueous solution&lt;/span&gt;&lt;/span&gt;
Authors: Suresh, S; Sugumar, R Wilfred; Maiyalagan, T
Abstract: &lt;span style="font-size:11.0pt;font-family:&#xD;
" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";mso-bidi-font-family:="" mangal;mso-ansi-language:en-gb;mso-fareast-language:en-us;mso-bidi-language:="" hi"="" lang="EN-GB"&gt;The adsorption characteristics of a low cost&#xD;
adsorbent prepared from &lt;i&gt;Curcuma angustifolia &lt;/i&gt;&lt;span style="mso-bidi-font-style:italic"&gt;scales (CA) for the removal of Basic&#xD;
Violet 14 from aqueous solution has been investigated. &lt;span style="mso-bidi-font-weight:&#xD;
bold"&gt;The experimental data have been analyzed by Langmuir, Freundlich and&#xD;
Temkin isotherm models. The results show that the adsorption isotherm is best&#xD;
defined by the Langmuir isotherm model and the adsorption capacity is found to&#xD;
be 208.33 mg/g for the prepared low cost adsorbent. The adsorption&#xD;
capacity of the prepared low cost adsorbent is superior compared with that of the&#xD;
adsorption capacity of calgon carbon. &lt;span style="font-size:&#xD;
11.0pt;font-family:" times="" new="" roman","serif";mso-fareast-font-family:+mn-ea;="" mso-bidi-font-family:mangal;mso-font-kerning:12.0pt;mso-ansi-language:en-gb;="" mso-fareast-language:en-us;mso-bidi-language:hi"="" lang="EN-GB"&gt;The kinetic data result at&#xD;
different concentrations have been analysed using pseudo first-order and&#xD;
pseudo-second order model. Boyd plot indicate that the adsorption of dye onto&#xD;
the low cost adsorbent and calgon carbon is controlled by film diffusion.&lt;span style="font-size:11.0pt;font-family:" times="" new="" roman","serif";="" mso-fareast-font-family:"times="" roman";mso-bidi-font-family:mangal;="" mso-ansi-language:en-gb;mso-fareast-language:en-us;mso-bidi-language:hi;="" mso-bidi-font-weight:bold"="" lang="EN-GB"&gt; Thermodynamic analysis indicate that the adsorption&#xD;
process is endothermic in nature. &lt;span style="font-size:&#xD;
11.0pt;font-family:" times="" new="" roman","serif";mso-fareast-font-family:"times="" roman";="" mso-bidi-font-family:mangal;mso-ansi-language:en-gb;mso-fareast-language:en-us;="" mso-bidi-language:hi"="" lang="EN-GB"&gt;The adsorbent is characterized&#xD;
by Fourier transformation infrared spectrometry (FTIR) and scanning electron&#xD;
microscopy (SEM). &lt;span style="mso-bidi-font-weight:bold"&gt;The material&#xD;
used in this study is an agricultural waste product, economical to use as an&#xD;
alternative to costlier adsorbents and can be an attractive option for dye&#xD;
removal in wastewater treatment processes in industries.&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;
Page(s): 368-378</description>
      <pubDate>Mon, 01 Sep 2014 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/32136</guid>
      <dc:date>2014-09-01T00:00:00Z</dc:date>
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