2012
DOI: 10.9734/acsj/2012/908
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Kinetic Study of Utilizing Groundnut Shell as an Adsorbent in Removing Chromium and Nickel from Dye Effluent

Abstract: Aims:To determine the adsorption of nickel and chromium in dye effluents using activated carbon prepared from groundnut shell and to determine the adsorption capacity at different contact time. Study Design: Adsorption capacity of the adsorbent.

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Cited by 44 publications
(20 citation statements)
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“…At the same time, the R 2 value(R= 0,934) of the pseudo-first-order cannot be neglected. It is sufficiently close to unity indicating that chemisorption and physisorption takes place concomitantly [21]. This conclusion is consistent to the results of isotherms and IR obtained above.…”
Section: Pseudo-second Order Modelsupporting
confidence: 91%
See 1 more Smart Citation
“…At the same time, the R 2 value(R= 0,934) of the pseudo-first-order cannot be neglected. It is sufficiently close to unity indicating that chemisorption and physisorption takes place concomitantly [21]. This conclusion is consistent to the results of isotherms and IR obtained above.…”
Section: Pseudo-second Order Modelsupporting
confidence: 91%
“…The quantity adsorbed seems to decrease with an increase in the adsorbent dose. This may be due to the aggregation on the adsorption sites as the amount of adsorbent increase [19,20,21,22]. The maximum quantity of Cu 2+ ions adsorbed at these conditions was 88,4 mg.g -1 with 0.025g of adsorbent.…”
Section: Effect Of the Adsorbent Dosementioning
confidence: 99%
“…In physical or thermal activation, the pyrolyzed carbon is exposed to an oxidizing atmosphere (such as CO 2 , steam or a mixture of both) in the temperature range of 600-1200°C and the porosity is developed by partial etching of the carbon. On the other hand, in chemical activation the carbon precursor is mixed with some chemicals such as NaOH [39], KOH [40][41][42][43][44][45][46][47][48], ZnCl 2 [5,[49][50][51], H 3 PO 4 [52][53][54] and H 2 SO 4 [3,55], and then carbonization and activation are accomplished simultaneously at a slightly lower temperature ranged within 300-950°C. Of the activating agents, KOH is the most promising because it can produce nanostructured porous carbons with higher yields at lower temperature, and produce materials with ultrahigh specific surface area up to 3000 m 2 g −1 with a well-defined pore size distribution.…”
Section: Synthesis Of Nanostructured Porous Carbons From Biomassmentioning
confidence: 99%
“…It has many forms or allotropes, which are widely used in many fields. Among them, porous carbon has been well developed and extensively utilized in modern industrial society due to its porous microstructure with immense surface area [2][3][4], high porosity along with good physiochemical stability [5,6], large adsorption capacity [7] and excellent reactivity [8][9][10]. However, the fabrication of such porous carbon faces some challenges as it is a complex and expensive synthesis process, involving high temperature and non-renewable precursors consequently limiting its commercial applications.…”
Section: Introductionmentioning
confidence: 99%
“…These are (i) bulk diffusion (ii) external mass transfer (film diffusion) (iii) chemical reaction (chemisorption) and (iv) inter-particle diffusion. These processes can act in series or parallel to account for the surface transport of a metal into an adsorbent [27]. The pseudo first-order and pseudo-second order kinetic models, and the Elovich model were enlisted to assess the nickel (II) adsorption mode (Figs.…”
Section: Kinetic Modeling Of Ni (Ii) Adsorptionmentioning
confidence: 99%