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    <link>http://localhost:8080/xmlui/handle/123456789/411</link>
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    <pubDate>Tue, 23 Jun 2026 06:26:55 GMT</pubDate>
    <dc:date>2026-06-23T06:26:55Z</dc:date>
    <item>
      <title>Sonochemical degradation of 3-methylpyridine (3MP) intensified using combination with various oxidants</title>
      <link>http://localhost:8080/xmlui/handle/123456789/3052</link>
      <description>Title: Sonochemical degradation of 3-methylpyridine (3MP) intensified using combination with various oxidants
Authors: Daware, Gaurav B.; Gogate, Parag R.
Abstract: 3-Methyl pyridine (3MP) is a toxic and hazardous organic compound having considerable negative impact on&#xD;
environment and living organisms. The objective of this work to report a novel treatment strategy based on&#xD;
sonochemical degradation of 3MP, in combination with oxidants such as hydrogen peroxide, Fenton’s reagent,&#xD;
peroxymonosulphate (PMS), and potassium persulphate (KPS) as well as solar irradiations. A bath sonicator&#xD;
operating at 25 kHz frequency and rated power dissipation of 100 W was applied in the work to study different&#xD;
approaches with an objective to enhance the removal of 3MP in lesser time. Effect of operating parameters such&#xD;
as pH (over the range of 2–10), treatment time, temperature (25–55 °C) and ultrasonic power (25 W to 150 W)&#xD;
on the degradation has been studied and the best conditions were used in subsequent combination approaches. It&#xD;
was demonstrated that ultrasound in combination with PMS, ferrous sulphate (FeSO4) and solar irradiations&#xD;
(approach of US/PMS/FeSO4/solar irradiation) is the best treatment strategy yielding maximum degradation as&#xD;
97.4% with highest cavitational yield as 1.920 × 10−4 mg/J and highest synergetic Index as 2.70. Kinetic&#xD;
analysis revealed that first order mechanism fitted well to all the approaches involving different combinations of&#xD;
ultrasound, oxidising agents and solar irradiation. Degradation products were also analysed that established the&#xD;
degradation mechanism as C2 and C3 ring cleavages forming 1, 4-dihydro3-methylpyridine followed by Levulinic&#xD;
acid as non -toxic main by-product. Overall the work clearly demonstrated an effective treatment approach&#xD;
involving combined sonication with oxidants for remediation of 3MP also providing insights on kinetics and&#xD;
mechanism of degradation.</description>
      <pubDate>Thu, 02 Apr 2020 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://localhost:8080/xmlui/handle/123456789/3052</guid>
      <dc:date>2020-04-02T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Adsorption of 3-Aminopyridine (3AP) from aqueous solution using sugarcane bagasse activated carbon (SBAC)</title>
      <link>http://localhost:8080/xmlui/handle/123456789/3047</link>
      <description>Title: Adsorption of 3-Aminopyridine (3AP) from aqueous solution using sugarcane bagasse activated carbon (SBAC)
Authors: Daware, Gaurav B.; Gogate, Parag R.
Abstract: Adsorption of 3-Aminopyridine (3AP) from simulated effluent using sugarcane bagasse&#xD;
activated carbon (SBAC) was studied based on batch and continuous operations. Characterization of synthesized SBAC was performed initially using BET and SEM analysis.&#xD;
Different batch experiments were performed to understand the effect of operating&#xD;
parameters such as initial concentration, pH, SBAC dose, time and temperature to&#xD;
understand the effect on the extent of adsorption. The maximum adsorption capacity for&#xD;
batch adsorption was established as 54.4 mg/g whereas the maximum extent of removal&#xD;
was 97.6 % under optimized conditions. The observed data at equilibrium was found to&#xD;
be best fitted to Freundlich and Langmuir adsorption isotherms. Kinetic study revealed&#xD;
that pseudo-second order mechanism prevailed. Desorption of 3AP using ethanol showed&#xD;
good reuse efficacy for five cycles. Column adsorption experiments were also performed&#xD;
under varying SBAC bed height, concentration of 3AP and volumetric flow rate of 3AP&#xD;
solution to determine the breakthrough parameters. The fitting of the Yoon–Nelson&#xD;
and Thomas adsorption models to the obtained breakthrough data was studied and&#xD;
found to be satisfactory. Maximum adsorption capacity of SBAC for adsorption of 3AP in&#xD;
continuous operation was established as 65.6 mg/g. The obtained results demonstrated&#xD;
very good performance of SBAC for effective removal of 3AP in both batch and column&#xD;
operations.</description>
      <pubDate>Sat, 23 May 2020 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://localhost:8080/xmlui/handle/123456789/3047</guid>
      <dc:date>2020-05-23T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Treatment of Dye Containing Real Industrial Efuents using NaOH‑Activated Ficus racemosa and Prunus dulcis based Novel Adsorbents</title>
      <link>http://localhost:8080/xmlui/handle/123456789/2818</link>
      <description>Title: Treatment of Dye Containing Real Industrial Efuents using NaOH‑Activated Ficus racemosa and Prunus dulcis based Novel Adsorbents
Authors: Jain, S. N.; Gogate, P. R.
Abstract: The present study aims at evaluating the potential of synthesized biosorbents using NaOH-activated dead leaves of Ficus racemosa (NTFR) and Prunus dulcis (NTPD) for the treatment of real industrial efuents containing dyes. Kinetic and isotherm&#xD;
studies have been performed to establish the important design-related information for the treatment of industrial efuent using&#xD;
synthesized biosorbents. The extent of dye removal obtained as 99.19% for the studies involving pure dye solution of Acid&#xD;
Blue 25 dye with 50 mg L−1 as initial concentration using NTFR biosorbent was found to decrease marginally to 96.72% in&#xD;
the case of real efuent with similar dye loading and under similar operating conditions. Biosorption capacity for the case&#xD;
of pure Acid Blue 25 dye solution obtained as 83.33 mg g−1 also marginally decreased to 80.65 mg g−1 for the industrial&#xD;
efuent. Similarly, for the case of Acid Green 25 dye, extent of dye removal obtained as 92.09% was found to decrease to&#xD;
84.51% in the case of mixed industrial efuent. In this case, reduction in chemical oxygen demand (COD) was also measured&#xD;
and compared with that of pure Acid Green 25 dye solution. COD reduction was obtained as 53.97% at the optimized dose&#xD;
of 18 g/L of NTPD for mixed industrial efuent which was lower than 92.05% obtained at the optimized biosorbent dose for&#xD;
pure Acid Green 25 dye solution. Langmuir and pseudo-second-order model ftted well to the obtained data in the present&#xD;
study. The obtained results confrmed potential of synthesized biosorbents for removal of dyes from industrial efuent and&#xD;
also established the infuence of other compounds present in the industrial efuent on removal rate of individual dyes.</description>
      <pubDate>Sun, 17 Feb 2019 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://localhost:8080/xmlui/handle/123456789/2818</guid>
      <dc:date>2019-02-17T00:00:00Z</dc:date>
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