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  <title>DSpace Collection:</title>
  <link rel="alternate" href="http://localhost:8080/xmlui/handle/123456789/2366" />
  <subtitle />
  <id>http://localhost:8080/xmlui/handle/123456789/2366</id>
  <updated>2026-06-23T06:34:15Z</updated>
  <dc:date>2026-06-23T06:34:15Z</dc:date>
  <entry>
    <title>Equilibrium and Kinetic Studies of Ni (II) Adsorption using Pineapple and Bamboo Stem Based Adsorbents</title>
    <link rel="alternate" href="http://localhost:8080/xmlui/handle/123456789/3815" />
    <author>
      <name />
    </author>
    <id>http://localhost:8080/xmlui/handle/123456789/3815</id>
    <updated>2025-07-31T04:58:54Z</updated>
    <published>2013-09-12T00:00:00Z</published>
    <summary type="text">Title: Equilibrium and Kinetic Studies of Ni (II) Adsorption using Pineapple and Bamboo Stem Based Adsorbents
Abstract: This work addresses the preparation and characterization of&#xD;
inexpensive adsorbents for the removal of Ni (II) from aqueous&#xD;
solutions. Activated carbon based adsorbents have been prepared&#xD;
from plant based biomass resources, namely Pineapple stem&#xD;
(Ananas Comosus) and Bamboo Stem (Bambuseae). Adopting&#xD;
phosphoric acid and heat treatment techniques, it has been&#xD;
observed that the bamboo stem activated charcoal (BSAC) and&#xD;
pineapple stem (PS) adsorbents had a BET surface area of 116&#xD;
and 11.47m2/g, respectively. FTIR analysis indicated that various&#xD;
surface functional groups (such as C≡N stretching, stretching&#xD;
vibration of C=O, –CH3 wagging and C–O stretching vibration)&#xD;
contribute towards Ni (II) adsorption. Batch mode adsorption&#xD;
experiments were conducted for these adsorbents in the range of&#xD;
50–300mg/L Ni (II) solution concentration, 2–10 pH, 15–300 min.&#xD;
contact time, and 0.02–0.1 g/50mL dosage. The BSAC adsorbent&#xD;
has been characterized with a metal uptake and %removal&#xD;
of 121.72 mg/g and 92.47, respectively, which corresponds to&#xD;
45% higher metal uptake than corresponding bamboo based&#xD;
adsorbents presented in the literature. Further experimentation&#xD;
with BSAC enabled to achieve activated charcoal with surface&#xD;
area values similar to that of the commercial activated carbon&#xD;
adsorbent. The bamboo adsorbent has also been evaluated to&#xD;
perform similar to the commercial activated carbon for the&#xD;
removal and recovery of Pd (II) from synthetic electroless plating&#xD;
solutions. Also, a conceptual cost analysis indicated and affirmed&#xD;
towards the potential of the BSAC adsorbents for waste water&#xD;
treatment applications.</summary>
    <dc:date>2013-09-12T00:00:00Z</dc:date>
  </entry>
  <entry>
    <title>Adsorption of 2-picoline from wastewater by agro coal ash: parametric, kinetic, equilibrium and thermodynamic features</title>
    <link rel="alternate" href="http://localhost:8080/xmlui/handle/123456789/2860" />
    <author>
      <name>Daware, G. B.</name>
    </author>
    <author>
      <name>Vijay Babu, P. V.</name>
    </author>
    <id>http://localhost:8080/xmlui/handle/123456789/2860</id>
    <updated>2020-12-10T10:35:54Z</updated>
    <published>2013-05-30T00:00:00Z</published>
    <summary type="text">Title: Adsorption of 2-picoline from wastewater by agro coal ash: parametric, kinetic, equilibrium and thermodynamic features
Authors: Daware, G. B.; Vijay Babu, P. V.
Abstract: 2-Picoline is a derivative of pyridine. Due to the hazardous nature, the removal of 2-picoline&#xD;
from wastewater is important. In the present study, the ability of agro coal ash as an&#xD;
adsorbent for the removal of 2-picoline from wastewater in a broad range of concentration&#xD;
(50–300 mg/L) was investigated. The influence of various experimental parameters like initial&#xD;
pH, adsorbent dose, contact time, initial concentration and temperature on the removal of&#xD;
2-picoline on agro coal ash were studied. The optimum conditions for the maximum removal&#xD;
of 2-picoline were found to be: initial pH 6, contact time = 7 h and adsorbent dose = 2 g/L.&#xD;
Adsorption of 2-picoline followed pseudo-second-order rate kinetics. The Langmuir and&#xD;
Freundlich adsorption equilibrium isotherm models were analysed. The values of the change&#xD;
in Gibb’s free energy (DG), enthalpy (DH) and entropy (DS) were calculated. Thermodynamic&#xD;
studies revealed that adsorption of 2-picoline on agro coal ash is an endothermic process.</summary>
    <dc:date>2013-05-30T00:00:00Z</dc:date>
  </entry>
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