2010
DOI: 10.1016/j.jcis.2009.11.070
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Adsorptive removal of dihydrogenphosphate ion from aqueous solutions using mono, di- and tri-ammonium-functionalized SBA-15

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Cited by 45 publications
(19 citation statements)
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“…The equilibrium model parameters are provided in Table 4. From the Langmuir model, Table 3 Kinetic model parameters obtained from model fitting to experimental data Mesoporous silica Dye Pseudo-first-order model Pseudo-second-order model Elovich model [6,22,25,29]. Additionally, the value of Q m for AB25 in f-MCM-41 was 45.9 mg g −1 , which was similar to or lower than other reported values (55.4 and 145 mg g −1 ) of functionalized mesoporous silica for AB [30,31].…”
Section: Kinetics Equilibrium Isotherms and Thermodynamic Analysessupporting
confidence: 66%
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“…The equilibrium model parameters are provided in Table 4. From the Langmuir model, Table 3 Kinetic model parameters obtained from model fitting to experimental data Mesoporous silica Dye Pseudo-first-order model Pseudo-second-order model Elovich model [6,22,25,29]. Additionally, the value of Q m for AB25 in f-MCM-41 was 45.9 mg g −1 , which was similar to or lower than other reported values (55.4 and 145 mg g −1 ) of functionalized mesoporous silica for AB [30,31].…”
Section: Kinetics Equilibrium Isotherms and Thermodynamic Analysessupporting
confidence: 66%
“…The negative values of ΔH˚repre-sent the exothermic nature of MB adsorption to MCM-41 and AB25 adsorption to f-MCM-41, indicating that adsorption capacity decreases with increasing temperature. The negative values of ΔS˚indicate that energy is released during the sorption process and randomness decreases at the interface between solid and solution [22]. In addition, the positive values of ΔG˚were obtained for MB adsorption to MCM-41 and AB25 adsorption to f-MCM-41 (Table 5).…”
Section: Kinetics Equilibrium Isotherms and Thermodynamic Analysesmentioning
confidence: 87%
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