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    <title>NOPR Collection:</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/15852</link>
    <description />
    <pubDate>Sat, 10 Oct 2026 04:32:52 GMT</pubDate>
    <dc:date>2026-10-10T04:32:52Z</dc:date>
    <item>
      <title>Vapor phase adsorption of xylene on granular activated carbon - Experimental and theoretical breakthrough curves</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/15864</link>
      <description>Title: Vapor phase adsorption of xylene on granular activated carbon - Experimental and theoretical breakthrough curves
Authors: Gupta, Kaushal Naresh; Rao, Nandagiri Jagannatha; Agarwal, Govind Kumar
Abstract: Experiments have been carried out to study&#xD;
adsorption of xylene (a volatile organic compound) on the granular activated&#xD;
carbon, using the experimental variables, such as inlet gas concentration (2400&#xD;
– 6200 ppm), gas flow rate (50 mL/min) and height of the adsorbent bed (0.015 –&#xD;
0.025 m). The breakthrough curves are then drawn between ratios of outlet gas&#xD;
concentration to inlet gas concentration and time for different operating&#xD;
conditions. A mathematical model is developed to predict the breakthrough&#xD;
curves of xylene on granular activated carbon. The model shows the effects of&#xD;
the gas-particle film mass transfer resistance, adsorbent pore diffusion and instantaneous&#xD;
local adsorption equilibrium at the pore surface. The experimental data and the&#xD;
corresponding model simulated results have been compared and are found to be in&#xD;
good agreement. The breakthrough time increases with increase in bed height and&#xD;
decreases with increase in inlet concentration.
Page(s): 26-32</description>
      <pubDate>Tue, 01 Jan 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/15864</guid>
      <dc:date>2013-01-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Equilibrium, kinetic and thermodynamic studies on biosorption of lead(II) and cadmium(II) from aqueous solution by polypores biomass</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/15863</link>
      <description>Title: Equilibrium, kinetic and thermodynamic studies on biosorption of lead(II) and cadmium(II) from aqueous solution by polypores biomass
Authors: Suguna, M; Kumar, N Siva
Abstract: &lt;span style="mso-bidi-font-weight:&#xD;
bold" lang="EN-GB"&gt;Polypores (woody pore fungi&lt;span style="mso-bidi-font-weight:bold"&gt;) biomass has been used as&#xD;
an biosorbent for the removal of Pb(II) and Cd(II) from aqueous solution under&#xD;
batch equilibrium experimental conditions. The resulting biosorbent is&#xD;
characterized by SEM and FTIR techniques. The effect of experimental&#xD;
parameters, such as solution &lt;i style="mso-bidi-font-style:&#xD;
normal"&gt;p&lt;/i&gt;H, biomass dosage, contact time, initial metal ion concentration&#xD;
and temperature of Pb(II) and Cd(II) have been evaluated on the metal uptake&#xD;
performance. The &lt;i style="mso-bidi-font-style:normal"&gt;p&lt;/i&gt;H for optimum&#xD;
biosorption is found to be 5.0 for Cd(II) (92.5% removal) and Pb(II) (96.4%&#xD;
removal)&lt;span style="mso-bidi-font-style:italic"&gt;. The adsorption kinetic&#xD;
data are best described by pseudo-second-order kinetic model with good&#xD;
correlation coefficient and low error function values. The experimental results&#xD;
indicate that the Langmuir isotherm describes the biosorption of&#xD;
Cd(II) and Pb(II) ions onto the biomass better than the Freundlich,&#xD;
Dubinin-Radushkevich (D-R) and Temkin models at all the temperatures studied.&#xD;
The calculated thermodynamic parameters (∆G&lt;sup&gt;o&lt;/sup&gt;, ∆H&lt;sup&gt;o&lt;/sup&gt; and ∆S&lt;sup&gt;o&lt;/sup&gt;)&#xD;
show that the biosorption of both metal ions is feasible,&#xD;
spontaneous and exothermic in nature at 303–313 K. Based on the results&#xD;
obtained such as good uptake capacity and its low cost, polypores&#xD;
biomass appears to be a promising biosorbent material for the removal of Cd(II)&#xD;
and Pb(II) ions from aqueous media.&#xD;
&#xD;
&lt;/span&gt;&lt;/span&gt;&lt;/span&gt;
Page(s): 57-69</description>
      <pubDate>Tue, 01 Jan 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/15863</guid>
      <dc:date>2013-01-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>&lt;span style="font-size:11.0pt;mso-bidi-font-size: 10.0pt;font-family:"Times New Roman";mso-fareast-font-family:"Times New Roman"; mso-ansi-language:EN-GB;mso-fareast-language:EN-US;mso-bidi-language:AR-SA" lang="EN-GB"&gt;Adsorption of Cu and Zn on calcium alginate immobilized &lt;i&gt;Penicillium sp&lt;/i&gt;.&lt;/span&gt;</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/15862</link>
      <description>Title: &lt;span style="font-size:11.0pt;mso-bidi-font-size: 10.0pt;font-family:"Times New Roman";mso-fareast-font-family:"Times New Roman"; mso-ansi-language:EN-GB;mso-fareast-language:EN-US;mso-bidi-language:AR-SA" lang="EN-GB"&gt;Adsorption of Cu and Zn on calcium alginate immobilized &lt;i&gt;Penicillium sp&lt;/i&gt;.&lt;/span&gt;
Authors: Mishra, S P
Abstract: Calcium alginate has been used for&#xD;
immobilization of &lt;i&gt;Penicillium sp. &lt;/i&gt;(PS). The bio granules thus prepared&#xD;
by the immobilization technique, i.e. immobilized PS (IPS), are then used for&#xD;
Cu and Zn sorption from waste water. Various sorption parameters are studied to&#xD;
establish the optimum sorption conditions. The study shows that 5.0 &lt;i style="mso-bidi-font-style:normal"&gt;p&lt;/i&gt;H and 200 min contact time are the&#xD;
optimum values for both Cu and Zn sorption. The activation energy for Cu&#xD;
sorption by IPS is found to be 19.4 kJ/mole and Zn sorption on IPS is found to&#xD;
be temperature independent. The sorption process obeys Freundlich sorption&#xD;
isotherm in both the cases. The sorption of Cu and Zn by IPS follows&#xD;
pseudo-first order reaction kinetics and is found to be diffusion controlled in&#xD;
nature. The dependence of the rate constant on different sorption parameters is&#xD;
observed and these dependence factors are included in the final rate&#xD;
expressions.
Page(s): 21-25</description>
      <pubDate>Tue, 01 Jan 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/15862</guid>
      <dc:date>2013-01-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Assessment of auto-oxidation cum self-heating tendency of  Indian coals by DRIFT studies</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/15861</link>
      <description>Title: Assessment of auto-oxidation cum self-heating tendency of  Indian coals by DRIFT studies
Authors: Khan, Samit; Adak, Ashis K; Sen, Raja; Sarkar, Abhijit
Abstract: Coal&#xD;
self-heating, due to low temperature oxidation of coal, is generally considered to be the primary cause of spontaneous&#xD;
ignition. With the purpose of having a more definitive&#xD;
quantization of this subtle stage of coal oxidation, study on proneness to coal&#xD;
towards auto-oxidation, vis-à-vis self-heating phenomenon, has been carried out.&#xD;
Various methods like crossing point temperature (CPT), diffuse reflectance infrared&#xD;
fourier transform spectroscopy (DRIFT), differential scanning calorimetry-thermogravimetric&#xD;
analysis (DSC-TGA) and wet oxidation method has been used for comparative study.&#xD;
&#xD;
It is observed that though CPT values alone are adequately indicative and are&#xD;
consistent with actual field experience, the combination of CPT and DRIFT data&#xD;
complements each other very well to provide greater information for better&#xD;
prediction of proneness to auto-oxidation vis-à-vis self-heating phenomenon of&#xD;
coals. Other methods tried are found to be comparatively inadequate.
Page(s): 52-56</description>
      <pubDate>Tue, 01 Jan 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/15861</guid>
      <dc:date>2013-01-01T00:00:00Z</dc:date>
    </item>
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