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    <link>http://localhost:8080/xmlui/handle/123456789/325</link>
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    <pubDate>Tue, 23 Jun 2026 06:26:44 GMT</pubDate>
    <dc:date>2026-06-23T06:26:44Z</dc:date>
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      <title>Ni(II) adsorption characteristics of commercial activated carbon from synthetic electroless plating solutions</title>
      <link>http://localhost:8080/xmlui/handle/123456789/3817</link>
      <description>Title: Ni(II) adsorption characteristics of commercial activated carbon from synthetic electroless plating solutions</description>
      <pubDate>Mon, 02 Nov 2015 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://localhost:8080/xmlui/handle/123456789/3817</guid>
      <dc:date>2015-11-02T00:00:00Z</dc:date>
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    <item>
      <title>NaOH-treated dead leaves of Ficus racemosa as an efficient biosorbent for Acid Blue 25 removal</title>
      <link>http://localhost:8080/xmlui/handle/123456789/2891</link>
      <description>Title: NaOH-treated dead leaves of Ficus racemosa as an efficient biosorbent for Acid Blue 25 removal
Authors: Jain, S. N.; Gogate, P. R.
Abstract: A novel biosorbent synthesized from Ficus&#xD;
racemosa leaves based on the treatment using NaOH was&#xD;
applied for removal of Acid Blue 25 from aqueous solution. The synthesized biosorbent was characterized using&#xD;
scanning electron microscopy, Fourier transform infrared&#xD;
spectroscopy and Brunauer–Emmett–Teller analysis.&#xD;
NaOH treatment was demonstrated to remove lignin content from the biomass and to induce the development of&#xD;
significant pores. Batch experiments were performed to&#xD;
evaluate the effect of important operating parameters such&#xD;
as pH (range of 2–10), biosorbent dose (range of 1–10 g/&#xD;
L), contact time (range of 0–5 h), initial dye concentration&#xD;
(range of 50–400 mg/L) and temperature (range of&#xD;
293–323 K) on the extent of removal of Acid Blue 25. The&#xD;
established optimum conditions were pH of 2, biosorbent&#xD;
dose of 4 g/L, contact time of 3 h and temperature of&#xD;
323 K, yielding maximum removal of dye. Pseudo-secondorder model was found to best fit the kinetic data. Langmuir and Temkin isotherm models were found to best fit&#xD;
the equilibrium data. The obtained thermodynamic&#xD;
parameters confirmed endothermic and spontaneous nature&#xD;
of adsorption. The study established the utility of novel&#xD;
biosorbent for removal of Acid Blue 25 with higher&#xD;
adsorption capacities (83.33 mg/g) as compared to the&#xD;
more commonly used adsorbents. Desorption-adsorption&#xD;
studies conducted for seven cycles indicated potential&#xD;
reusability of synthesized biosorbent for the treatment of&#xD;
dye effluents.</description>
      <pubDate>Tue, 31 May 2016 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://localhost:8080/xmlui/handle/123456789/2891</guid>
      <dc:date>2016-05-31T00:00:00Z</dc:date>
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    <item>
      <title>Fixed bed column study for the removal of Acid Blue 25 dye using NaOH-treated fallen leaves of Ficus racemosa</title>
      <link>http://localhost:8080/xmlui/handle/123456789/2224</link>
      <description>Title: Fixed bed column study for the removal of Acid Blue 25 dye using NaOH-treated fallen leaves of Ficus racemosa
Authors: Jain, Suyog N; Gogate*, Parag R.
Abstract: The present study aims at evaluating the potential of adsorbent obtained from fallen leaves of&#xD;
Ficus racemosa with NaOH activation for Acid Blue 25 (AB 25) dye removal from aqueous solution&#xD;
in a continuous mode. The effect of various operating parameters such as bed height (2–6 cm),&#xD;
initial dye concentration (50–200 mg/L) and flow rate (6–10 mL/min) on the extent of dye removal&#xD;
has been investigated. The obtained results for the variation of operating parameters confirmed&#xD;
better column performance at higher bed height and lower flow rate. Different kinetic models&#xD;
such as Thomas, Adams–Bohart, Yoon–Nelson and bed depth service time (BDST) were applied&#xD;
to the obtained experimental data using column studies to predict the breakthrough curves and&#xD;
average mean square error has been employed to check the best suitability of the model. Thomas&#xD;
and BDST model predictions were established to be in better agreement with the experimental&#xD;
results. Maximum biosorption capacity for 100 mg/L of dye concentration present initially was&#xD;
obtained as 44.14 mg/g at optimum condition of 6 mL/min as the flow rate. The experimental&#xD;
observed capacity matched with the predicted biosorption capacity of 45.71 mg/g using the&#xD;
Thomas model. Elution studies conducted for seven cycles confirmed the reusability of synthesized&#xD;
biosorbent to treat industrial dye effluent in a column. Overall, the study clearly established&#xD;
the utility of synthesized biosorbent for the removal of AB 25 from wastewater in a continuous&#xD;
fixed bed adsorption process.</description>
      <pubDate>Thu, 13 Jul 2017 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://localhost:8080/xmlui/handle/123456789/2224</guid>
      <dc:date>2017-07-13T00:00:00Z</dc:date>
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