Adsorption of Zn(II) in aqueous solution by activated carbons prepared from evergreen oak (Quercus rotundifolia L.)

被引:42
作者
del Mar Gomez-Tamayo, M. [2 ]
Macias-Garcia, Antonio [2 ]
Diaz Diez, M. Angeles [2 ]
Cuerda-Correa, Eduardo M. [1 ]
机构
[1] Univ Extremadura, Dept Inorgan Chem, Fac Sci, E-06071 Badajoz, Spain
[2] Univ Extremadura, Dept Elect & Electromech Engn, Area Mat Sci, Sch Ind Engn, E-06071 Badajoz, Spain
关键词
activated carbon; evergreen oak; phosphoric acid activation; zinc removal; adsorption in liquid phase;
D O I
10.1016/j.jhazmat.2007.08.012
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In the present work activated carbons have been prepared from evergreen oak wood. Different samples have been prepared varying the concentration of the activating agent (H3PO4) and the treatment temperature. The yield of the process decreases with increasing phosphoric acid concentrations. Furthermore, high concentrations of activating agent lead to mainly mesoporous activated carbons to the detriment of the microporous texture. Treatment temperatures up to 450 degrees C lead to a progressive increase of the micro- and mesopore volumes. Values of specific surface area (S-BET) as high as 1723 m(2) g(-1) have been obtained using appropriate phosphoric acid concentrations and treatment temperatures. The samples prepared have been successfully used in the removal of Zn(II) from aqueous solutions. From the adsorption kinetic data it may be stated that the equilibrium time is, in all cases, below 170 h. The adsorption process as a rule becomes faster as the mesopore volume and specific surface area of the samples increase. The adsorption isotherms in liquid phase point out that the adsorption capacity (n(0)(s)) and the affinity towards the solute (K-ci) are higher for the sample showing the most developed mesoporous texture and surface area as well. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:28 / 36
页数:9
相关论文
共 42 条
[11]   Catalysed and uncatalysed steam gasification of eucalyptus char:: influence of variables and kinetic study [J].
Encinar, JM ;
González, JF ;
Rodríguez, JJ ;
Ramiro, MJ .
FUEL, 2001, 80 (14) :2025-2036
[12]   Characterization of burning and CO2 gasification of chars from mixtures of Zonguldak (Turkey) and Australian bituminous coals [J].
Erincin, D ;
Sinag, A ;
Misirhoglu, Z ;
Canel, M .
ENERGY CONVERSION AND MANAGEMENT, 2005, 46 (17) :2748-2761
[13]   FLUIDS IN NARROW PORES - ADSORPTION, CAPILLARY CONDENSATION, AND CRITICAL-POINTS [J].
EVANS, R ;
MARCONI, UMB ;
TARAZONA, P .
JOURNAL OF CHEMICAL PHYSICS, 1986, 84 (04) :2376-2399
[14]   Hydrogen adsorption by nanostructured carbons synthesized by chemical activation [J].
Figueroa-Torres, M. Zyzlila ;
Robau-Sanchez, Alejandro ;
De la Torre-Saenz, Luis ;
Aguilar-Elguezabal, Alfredo .
MICROPOROUS AND MESOPOROUS MATERIALS, 2007, 98 (1-3) :89-93
[15]   GENERAL TREATMENT AND CLASSIFICATION OF SOLUTE ADSORPTION-ISOTHERM .1. THEORETICAL [J].
GILES, CH ;
SMITH, D ;
HUITSON, A .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1974, 47 (03) :755-765
[16]   Adsorption of mercury, cadmium and lead from aqueous solution on heat-treated and sulphurized activated carbon [J].
Gomez-Serrano, V ;
Macias-Garcia, A ;
Espinosa-Mansilla, A ;
Valenzuela-Calahorro, C .
WATER RESEARCH, 1998, 32 (01) :1-4
[17]  
Greenwood N. N., 1989, CHEM ELEMENTS
[18]   Yields and CO2 reactivity of chars from almond shells obtained by a two heating step carbonisation process.: Effect of different chemical pre-treatments and ash content [J].
Iniesta, E ;
Sánchez, F ;
García, AN ;
Marcilla, A .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2001, 58 :983-994
[19]   Activated carbons from yellow poplar and white oak by H3PO4 activation [J].
Jagtoyen, M ;
Derbyshire, F .
CARBON, 1998, 36 (7-8) :1085-1097
[20]  
Kaim W., 2001, BIOINORGANIC CHEM IN, P242