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Ammonium-functionalized mesoporous silica MCM-41 for phosphate removal from aqueous solutions

Authors
Kang, Jin-KyuKim, Jae-HyunKim, Song-BaeLee, Sang-HyupChoi, Jae-WooLee, Chang-Gu
Issue Date
14-5월-2016
Publisher
DESALINATION PUBL
Keywords
Mesoporous silica; MCM-41; Phosphate; Sorption; Surface functionalization
Citation
DESALINATION AND WATER TREATMENT, v.57, no.23, pp.10839 - 10849
Indexed
SCIE
SCOPUS
Journal Title
DESALINATION AND WATER TREATMENT
Volume
57
Number
23
Start Page
10839
End Page
10849
URI
https://scholar.korea.ac.kr/handle/2021.sw.korea/88653
DOI
10.1080/19443994.2015.1038590
ISSN
1944-3994
Abstract
The aim of this study was to investigate the removal of phosphate (P) using ammonium-functionalized MCM-41 (A-MCM-41). Batch experiments were performed with A-MCM-41 under various conditions including the adsorbent dose, reaction time, initial P concentration, and solution pH. The results showed that the phosphate removal in the MCM-41 (initial P conc.=2mgPL(-1)) was negligible with the percent removal of 1.0% at the adsorbent dosages between 0.5 and 2.0gL(-1). In the case of A-MCM-41, the percent removal increased from 73.6 to 100% as the adsorbent dose increased from 0.5 to 2.0gL(-1). This indicated an enhancement of the phosphate removal due to the surface modification of the MCM-41 through the functionalization of the ammonium group (NH3+). The results also demonstrated that the phosphate removal by the MCM-41 was minimal throughout the acidic and alkaline pH conditions (3.1% at pH 3.5; 1.0% at pH 5.4-10.7), whereas the phosphate removal by the A-MCM-41 was effective throughout the acidic and neutral pH values (94.7-97.6% at pH 3.5-7.4). In highly alkaline conditions, however, the phosphate removal by the A-MCM-41 was greatly reduced (3.4% at pH 10.7) due to the competition of the hydroxyl groups (OH-) with phosphate ions for sorption sites. The results indicated that the pseudo-second-order model was most suitable for describing the kinetic data with the parameter values of q(e)=1.86mgPg(-1) and k(2)=183.98gmgP(-1)h(-1). The Redlich-Peterson isotherm fits well with the equilibrium data, with the parameter values of K-R/a(R)=7.90mgPg(-1) and g=0.83.
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