A comparative adsorption study of β-naphthol on four polymeric adsorbents from aqueous solutions

被引:10
作者
Huang, Jianhan [1 ,2 ,3 ]
Yuan, Bin [2 ]
Wu, Xiaofei [2 ]
Deng, Shuguang [2 ]
机构
[1] Cent S Univ, Sch Chem & Chem Engn, Changsha 410083, Hunan, Peoples R China
[2] New Mexico State Univ, Dept Chem Engn, Las Cruces, NM 88003 USA
[3] Minist Educ, Key Lab Resources Chem Nonferrous Met, Changsha 410083, Hunan, Peoples R China
基金
中国国家自然科学基金;
关键词
Adsorption; Equilibria; Isosteric adsorption enthalpy; Kinetics; Column dynamics; SOLID-PHASE EXTRACTION; LINKED POLYSTYRENE; AMBERLITE XAD-4; PHENOL; RESIN; ISOTHERM; REMOVAL; WATER; THERMODYNAMICS; BREAKTHROUGH;
D O I
10.1016/j.jcis.2012.05.022
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Adsorptive removal of aromatic compounds from aqueous solutions by polymeric adsorbents has attracted many concerns in recent years. A comparative adsorption study including equilibria, kinetics and column dynamics of beta-naphthol from aqueous solutions was carried out using two hypercrosslinked polymeric adsorbents (HJ-1 and TEPA) we developed and two commercial polymeric adsorbents (XAD-4 and XAD-7). The adsorption isotherms could be well described by the Freundlich equation, and the adsorption equilibrium capacities of beta-naphthol followed an order of q(e(TEPA)) > q(e(HJ-1)) > q(e(XAD-4)) > q(e(XAD-7)). The isosteric adsorption enthalpies on HJ-1 and TEPA decreased with increasing adsorption fractional loading, while a constant enthalpy was observed for XAD-4 and XAD-7, implying that HJ-1 and TEPA had a heterogeneous surface while XAD-4 and XAD-7 possessed a homogenous surface. The surface energetic heterogeneity of HJ-1 and TEPA could be well characterized by the Do's model. The adsorption kinetics were fitted by both pseudo-first-order and pseudo-second-order rate equations, and the intra-particle diffusion was found to be the rate-limiting step. The adsorption breakthrough data were well correlated by the Thomas and Clark models, and the dynamic capacities for TEPA, XAD-4 and XAD-7 adsorbents were calculated to be 341.7, 321.6, 268.0 and 173.8 mg/g dry resin, which were within 90% of the corresponding equilibrium capacities obtained in the batch experiments. (C) 2012 Elsevier Inc. All rights reserved.
引用
收藏
页码:166 / 172
页数:7
相关论文
共 39 条
[1]   Kinetic and thermodynamics of chromium ions adsorption onto low-cost dolomite adsorbent [J].
Albadarin, Ahmad B. ;
Mangwandi, Chirangano ;
Al-Muhtaseb, Ala'a H. ;
Walker, Gavin M. ;
Allen, Stephen J. ;
Ahmad, Mohammad N. M. .
CHEMICAL ENGINEERING JOURNAL, 2012, 179 :193-202
[2]   Adsorption of 4-chlorophenol from aqueous solutions by xad-4 resin: Isotherm, kinetic, and thermodynamic analysis [J].
Bilgili, M. Sinan .
JOURNAL OF HAZARDOUS MATERIALS, 2006, 137 (01) :157-164
[3]   THE EXCHANGE ADSORPTION OF IONS FROM AQUEOUS SOLUTIONS BY ORGANIC ZEOLITES .2. [J].
BOYD, GE ;
ADAMSON, AW ;
MYERS, LS .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1947, 69 (11) :2836-2848
[5]   A REVIEW OF THE USE OF XAD RESINS TO CONCENTRATE ORGANIC-COMPOUNDS IN WATER [J].
DAIGNAULT, SA ;
NOOT, DK ;
WILLIAMS, DT ;
HUCK, PM .
WATER RESEARCH, 1988, 22 (07) :803-813
[6]   Hypercross-linked polystyrene and its potentials for liquid chromatography: a mini-review [J].
Davankov, V ;
Tsyurupa, M ;
Ilyin, M ;
Pavlova, L .
JOURNAL OF CHROMATOGRAPHY A, 2002, 965 (1-2) :65-73
[7]   A new adsorption isotherm for heterogeneous adsorbent based on the isosteric heat as a function of loading [J].
Do, DD ;
Do, HD .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (02) :297-310
[8]   Removal of common pharmaceuticals present in surface waters by Amberlite XAD-7 acrylic-ester-resin: Influence of pH and presence of other drugs [J].
Dominguez, Joaquin R. ;
Gonzalez, Teresa ;
Palo, Patricia ;
Cuerda-Correa, Eduardo M. .
DESALINATION, 2011, 269 (1-3) :231-238
[9]   Separation of Malachite Green and Methyl Green cationic dyes from aqueous medium by adsorption on Amberlite XAD-2 and XAD-4 resins using sodium dodecylsulfate as carrier [J].
dos Reis, Luis Gustavo T. ;
Robaina, Nicolle F. ;
Pacheco, Wagner F. ;
Cassella, Ricardo J. .
CHEMICAL ENGINEERING JOURNAL, 2011, 171 (02) :532-540
[10]  
Duong D.D., 1998, ADSORPTION ANAL EQUI