2017
DOI: 10.5004/dwt.2017.21480
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Removal of chromium from contaminated liquid effluents using natural brushite obtained from bovine bone

Abstract: a b s t r a c tNatural brushite (nDCPD) obtained from bovine bone was used to remove Cr(III) from aqueous solutions. Cr(III) adsorption was performed, varying adsorbent concentration and contact time in solution. The kinetic study of Cr(III) adsorption was performed with the kinetic models of pseudo-first order and pseudo-second order, Elovich, intraparticle and external diffusions. The experimental data were examined with the Langmuir, Freundlich, Redlich-Peterson (R-P), SIPS and Temkin isothermal models. The… Show more

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Cited by 5 publications
(8 citation statements)
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“…By having excellent surface area 3231.8 m 2 /, it confirmed a great adsorption capacity of the sorbent regarding the eradication of antibiotics pollutants namely sulfamethazine and chloramphenicol by around 1194 mg/g and 1240 mg/g, respectively [39]. Thus the brushite sorbent derived from bovine bone which was used to separate Cr(III) metal ions from aqueous solutions could reach up to 95% of pollutant removal [86]. All those reports agreed with the potentiality of bovine bone as an alternative option for greener sorbent.…”
Section: Bovine Bonementioning
confidence: 70%
“…By having excellent surface area 3231.8 m 2 /, it confirmed a great adsorption capacity of the sorbent regarding the eradication of antibiotics pollutants namely sulfamethazine and chloramphenicol by around 1194 mg/g and 1240 mg/g, respectively [39]. Thus the brushite sorbent derived from bovine bone which was used to separate Cr(III) metal ions from aqueous solutions could reach up to 95% of pollutant removal [86]. All those reports agreed with the potentiality of bovine bone as an alternative option for greener sorbent.…”
Section: Bovine Bonementioning
confidence: 70%
“…9, where C 0 is the initial concentration in mg L -1 and K L is the Langmuir constant. The value of R L lies between 0 and 1 indicating that the adsorption is favorable, while R L greater than 1 represents unfavorable adsorption and R L = 1 represents linear adsorption, while the adsorption process is irreversible if R L = 0 [36]. Fig.…”
Section: ∆Gmentioning
confidence: 99%
“…From these data, it can be observed that for both samples the process is spontaneous (∆G < 0) and that the Gibbs free energy increases with increasing temperature; this change is more noticeable for the GAC adsorbent while for PAC the increase is gradual. DNS adsorption has an endothermic nature (∆H > 0), which indicates that as the temperature increases, the adsorption capacity of GAC and PAC increases, which suggests that the electrostatic forces that are established on the surface of the adsorbent intervene significantly in the process [21]; on the other hand, with the change in entropy (∆S > 0) the randomness in the solid-fluid interface increases during the adsorption process, which is expected behavior for adsorption processes in the liquid phase [12,14,25,26,38].…”
Section: Dns Adsorption Thermodynamicsmentioning
confidence: 99%
“…This study showed that one of the causes for which there is a greater adsorption capacity and percentage of removal of DNS is the use of powdered AC, since it only depends on the participation of the functional groups that are found on the surface; conversely, for Figure 5 is constructed by comparing q vs t 0.5 , which refers to the intraparticle mass transfer model [14,28]. In Figure 5a, only two stages can be seen: external diffusion and equilibrium, since the intraparticle diffusion stage is not clearly observed [22,27,28,36].…”
Section: Mass Transfer Study On Dns Adsorption In Gac and Pacmentioning
confidence: 99%
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