Activated carbons prepared from wood particleboard wastes: Characterisation and phenol adsorption capacities

被引:197
作者
Girods, P. [2 ]
Dufour, A. [2 ]
Fierro, V. [3 ]
Rogaume, Y. [2 ]
Rogaume, C. [2 ]
Zoulalian, A. [2 ]
Celzard, A. [1 ]
机构
[1] Nancy Univ, LCSM, CNRS, ENSTIB 27,UMR 7555, F-88051 Epinal 9, France
[2] Nancy Univ, LERMAB, INRA, UMR 1093,ENGREF,ENSTIB 27, F-88051 Epinal 9, France
[3] Nancy Univ, LCSM, CNRS, UMR 7555, F-54506 Vandoeuvre Les Nancy, France
关键词
Activated carbons; Microporosity; Phenol adsorption; Waste disposal; Particleboards; SURFACE-CHEMISTRY; AQUEOUS-SOLUTIONS; UREA-FORMALDEHYDE; GENERAL TREATMENT; FLY-ASH; REMOVAL; HETEROGENEITY; WATER; EQUILIBRIUM; MECHANISM;
D O I
10.1016/j.jhazmat.2008.11.047
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The problems of valorisation of particleboard wastes on one hand, and contamination of aqueous effluents by phenolic compounds on the other hand, are simultaneously considered in this work. Preparation of activated carbons from a two steps thermo-chemical process, formerly designed for generating combustible gases, is suggested. The resultant carbonaceous residue is activated with steam at 800 degrees C. Depending on the preparation conditions, surface areas within the range 800-1300 m(2)/g are obtained, close to that of a commercial activated carbon (CAC) specially designed for water treatment and used as a reference material. The present work shows that particleboard waste-derived activated carbons (WAC) are efficient adsorbents for the removal of phenol from aqueous solutions, with maximum measured capacities close to 500 mg/g. However, most of times, the adsorption capacities are slightly lower than that of the commercial material in the same conditions, i.e., at equilibrium phenol concentrations below 300 ppm. Given the extremely low cost of activated carbons prepared from particleboard waste, it should not be a problem to use it in somewhat higher amounts than what is required with a more expensive commercial material. Phenol adsorption isotherms at 298 K were correctly fitted by various equations modelling type I and type 11 isotherms for CAC and WAC, respectively. Phenol adsorption isotherms of type 11 were justified by a 3-stages adsorption mechanism. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:491 / 501
页数:11
相关论文
共 60 条
[1]   Effect of texture and surface chemistry on adsorptive capacities of activated carbons for phenolic compounds removal [J].
Ania, CO ;
Parra, JB ;
Pis, JJ .
FUEL PROCESSING TECHNOLOGY, 2002, 77 :337-343
[2]  
[Anonymous], CHEMOSPHERE, DOI [10.1016/S0045-6535(98)00140-4, DOI 10.1016/S0045-6535(98)00140-4]
[3]   Adsorption of phenol by bentonite [J].
Banat, FA ;
Al-Bashir, B ;
Al-Asheh, S ;
Hayajneh, O .
ENVIRONMENTAL POLLUTION, 2000, 107 (03) :391-398
[4]  
Barton SS, 1997, POL J CHEM, V71, P651
[5]  
BENRACHEDI K, 1999, EAU I NUISANCES, V219, P54
[6]   Characterization of inorganic carbon-supported microfiltration and ultrafiltration membranes by aqueous phenol adsorption [J].
Bialopiotrowicz, T ;
Blanpain-Avet, P ;
Lalande, M .
SEPARATION SCIENCE AND TECHNOLOGY, 1999, 34 (09) :1803-1818
[7]   Modified active carbons from precursors enriched with nitrogen functions: sulfur removal capabilities [J].
Bimer, J ;
Satbut, PD ;
Bertozecki, S ;
Boudou, JP ;
Broniek, E ;
Siemieniewska, T .
FUEL, 1998, 77 (06) :519-525
[8]   Adsorption of gases in multimolecular layers [J].
Brunauer, S ;
Emmett, PH ;
Teller, E .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1938, 60 :309-319
[9]  
Brunauer S., 1945, ADSORPTION GASES VAP, V1
[10]  
BURG P, 2005, ACTUALITE CHIMIQUE N, V295, P91