Removal of ammonia from aqueous solutions by ligand exchange onto a Cu(II)-loaded chelating resin: kinetics, equilibrium and thermodynamics

被引:18
作者
Chen, Quanzhou [1 ,2 ]
Zhou, Kanggen [1 ,2 ]
Chen, Yan [1 ,2 ]
Wang, Aihe [1 ,2 ]
Liu, Fang [1 ,2 ]
机构
[1] Cent S Univ, Sch Met & Environm, Dept Environm Engn, Changsha 410083, Hunan, Peoples R China
[2] Chinese Natl Engn Res Ctr Control & Treatment Hea, Changsha 410083, Hunan, Peoples R China
基金
中国国家自然科学基金;
关键词
MICROBIAL FUEL-CELLS; SWINE WASTE-WATER; ION-EXCHANGE; ADSORPTION EQUILIBRIUM; LANDFILL LEACHATE; HYDROGEN-SULFIDE; NITROGEN REMOVAL; METHYLENE-BLUE; DYES; NITRIFICATION;
D O I
10.1039/c6ra28287c
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A poly ligand exchanger (PLE), Cu(II)-loaded chelating resin (ammonia adsorption reagent, named AMAR) was prepared to efficiently remove ammonia from solutions by ligand exchange. The kinetics, equilibrium and thermodynamics of the ligand sorption of ammonia onto AMAR from the synthesized solution were investigated under different experimental conditions. AMAR was characterized using FT-IR and a Micromeritics ASAP2020 surface area and porosity analyzer. The FT-IR analysis and pore textural property studies verified the functional group of weak iminodiacetate acid and reveal the combination form of Cu(II) with AMAR. The batch experiments with respect to different solution pHs, temperatures, initial ammonia concentrations and contact times were investigated. The equilibrium sorption experiments suggested that the optimum pH for ammonia adsorption was 9.5. The ammonia adsorption capacity on AMAR increased with the increase of contact time and initial ammonia concentration and decreased with the increase of temperature. The Langmuir (R-2 > 0.99) isotherm model was the best fitted model compared with the Freundlich model (R-2 > 0.91). The kinetic data were fitted well with the pseudo-second-order model compared with the pseudo-first-order and intra-particle models. The kinetic data confirmed that particle diffusion is not the only rate-limiting step in the adsorption process. The adsorption process might be affected by a variety of mechanisms. The maximum adsorption capacity was 42.735 mg g (-1), indicating that AMAR was a promising and efficient ammonia adsorption reagent.
引用
收藏
页码:12812 / 12823
页数:12
相关论文
共 82 条
[1]  
Alexandre VMF, 2016, ENVIRON TECHNOL, P1
[2]   Kinetics and equilibrium studies for the removal of nickel and zinc from aqueous solutions by ion exchange resins [J].
Alyuz, Bilge ;
Veli, Sevil .
JOURNAL OF HAZARDOUS MATERIALS, 2009, 167 (1-3) :482-488
[3]   Selective removal of arsenate from drinking water using a polymeric ligand exchanger [J].
An, B ;
Steinwinder, TR ;
Zhao, DY .
WATER RESEARCH, 2005, 39 (20) :4993-5004
[4]   Binding of Zn(II) Ions to Chitosan-PVA Blend in Aqueous Environment: Adsorption Kinetics and Equilibrium Studies [J].
Anitha, T. ;
Kumar, P. Senthil ;
Kumar, K. Sathish .
ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 2015, 34 (01) :15-22
[5]   On the removal of some phenolic compounds from aqueous solutions by using a sporopollenin-based ligand-exchange fixed bed -: Isotherm analysis [J].
Ayar, Ahmet ;
Gursal, Selpic ;
Gurten, A. Ali ;
Gezici, Orhan .
DESALINATION, 2008, 219 (1-3) :160-170
[6]   Removal of phosphate using copper-loaded polymeric ligand exchanger prepared by radiation grafting of polypropylene/polyethylene (PP/PE) nonwoven fabric [J].
Barsbay, Murat ;
Kavakli, Pinar Akkas ;
Guven, Olgun .
RADIATION PHYSICS AND CHEMISTRY, 2010, 79 (03) :227-232
[7]   Adsorption kinetics and thermodynamic parameters of cationic dyes from aqueous solutions by using a new strong cation-exchange resin [J].
Bayramoglu, Gulay ;
Altintas, Begum ;
Arica, M. Yakup .
CHEMICAL ENGINEERING JOURNAL, 2009, 152 (2-3) :339-346
[8]   Breakpoint chlorination and free-chlorine contact time:: Implications for drinking water N-nitrosodimethylamine concentrations [J].
Charrois, Jeffrey W. A. ;
Hrudey, Steve E. .
WATER RESEARCH, 2007, 41 (03) :674-682
[9]   Impact resistance of different factors on ammonia removal by heterotrophic nitrification-aerobic denitrification bacterium Aeromonas sp HN-02 [J].
Chen, Maoxia ;
Wang, Wenchao ;
Feng, Ye ;
Zhu, Xiaohua ;
Zhou, Houzhen ;
Tan, Zhouliang ;
Li, Xudong .
BIORESOURCE TECHNOLOGY, 2014, 167 :456-461
[10]  
Chen Q., 2016, WATER SCI TECHNOL