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首页> 外文期刊>Chemical engineering journal >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
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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

机译:由巴西松果壳制备的碳吸附剂用于从水溶液中去除Procion Red MX 3B的动力学,平衡和热力学研究

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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 usingC-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.
机译:从巴西松果壳(Araucaria angustifolia)制备了活性(AC-PW)和非活性(C-PW)碳质材料,并测试了其作为吸附剂的去除中的Procion Red MX 3B染料(PR-3B)的能力。水性废水。与C-PW相比,活化过程导致AC-PW吸附剂的比表面积,平均孔体积和平均孔径增加。研究了振荡时间,吸附剂用量和pH值对吸附量的影响。对于C-PW,pH范围从2.0到3.0,对于AC-PW,PR-3B的吸收范围从2.0到7.0是有利的。使用C-PW和AC-PW作为吸附剂达到平衡所需的接触时间分别为298 K和6 h。分数阶动力学模型的函数误差(F_(error))的值至少比使用伪一阶,伪二阶和Elovich动力学模型获得的值低15倍,表明该动力学模型是更好地拟合实验结果。对于平衡数据,Sips等温线模型的F_(误差)值比使用C-PW和AC-PW作为吸附剂的Langmuir,Freundlich和Redlich-Peterson等温线模型的值至少低4.0。 PR-3B的吸附焓和熵是通过298至323 K的吸附实验获得的。模拟的染厂废水用于检查所提出的碳在废水处理中的适用性。

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