Application of carbon adsorbents prepared from the Brazilian pine-fruit-shell for the removal of Procion Red MX 3B from aqueous solution-Kinetic, equilibrium, and thermodynamic studies

被引:155
作者
Calvete, Tatiana [1 ]
Lima, Eder C. [1 ]
Cardoso, Natali F. [1 ]
Dias, Silvio L. P. [1 ]
Pavan, Flavio A. [2 ]
机构
[1] Univ Fed Rio Grande do Sul, Inst Chem, BR-91501907 Porto Alegre, RS, Brazil
[2] UNIPAMPA, Fed Univ Pampa, Bage, RS, Brazil
关键词
Adsorption; Brazilian pine-fruit-shell; Activated carbon; Procion Red MX 3B dye; Simulated dyehouse effluent; METHYLENE-BLUE BIOSORPTION; YELLOW PASSION-FRUIT; STATISTICAL DESIGN; ACTIVATED CARBON; BATCH CONDITIONS; PECAN NUTSHELL; REACTIVE DYES; ANIONIC DYES; ADSORPTION; BIOSORBENT;
D O I
10.1016/j.cej.2009.08.019
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Activated (AC-PW) and non-activated (C-PW) carbonaceous materials were prepared from the Brazilian pine-fruit-shell (Araucaria angustifolia) and tested as adsorbents for the removal of Procion Red MX 3B dye (PR-3B) from aqueous effluents. The activation process lead to increase in the specific surface area, average porous volume, and average porous diameter of the adsorbent AC-PW when compared to C-PW. The effects of shaking time, adsorbent dosage and pH on adsorption capacity were studied. PR-3B uptake was favorable at pHs ranging from 2.0 to 3.0 for C-PW and 2.0 to 7.0 for AC-PW. The contact time required to obtain the equilibrium using C-PW and AC-PW as adsorbents was 6 and 4 h at 298 K, respectively. The values of the function error (F-error) of fractionary-order kinetic model was at least 15 times lower than the values obtained with pseudo-first-order, pseudo-second order and Elovich kinetic models, indicating that this kinetic model was better fitted to the experimental results. For equilibrium data the F-error values of the Sips isotherm model were at least 4.0 lower than the values of Langmuir, Freundlich, and Redlich-Peterson isotherm models using C-PW and AC-PW as adsorbents. The enthalpy and entropy of adsorption of PR-3B were obtained from adsorption experiments ranging from 298 to 323 K. Simulated dyehouse effluents were used to check the applicability of the proposed carbons for effluent treatment. (C) 2009 Elsevier B. V. All rights reserved.
引用
收藏
页码:627 / 636
页数:10
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