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Kinetics and thermodynamics studies of chromium(VI) ions adsorption onto activated carbon from aqueous solutions

机译:铬(VI)离子吸附在水溶液中活性炭中的动力学和热力学研究

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The removal of chromium(VI) from aqueous solutions by activated carbon has been investigated as a function of solution pH, initial chromium concentration C, solid/liquid ratio R and temperature T, The Freundlich and the Langmuir models have been applied and the equilibrium adsorption was found to best fit the Langmuir adsorption isotherm, where good correlation between theoretical and experimental equilibrium concentration of chromium(VI) ion was observed in most cases. The uptake distribution coefficient, K_D indicated that the chromium(VI) removal was the highest at minimum solid-liquid ratio. An empirical modelling was performed by using a 2~4 full factorial design, and regression equation for adsorption chromium(VI) was determined from the data. The pH and the temperature are the most significant parameter affecting chromium(VI) adsorption, followed by the solid/liquid ratio whereas the initial chromium(VI) concentration has the most negative effect on the process. However, the interaction pH—solid-liquid ratio—temperature has a positive effect. The optimal parameters obtained, pH 3.62; C=77.35 mg/L; R= 10 and T=45 °C, have been applied to wastewater from the tannery plant of Rouiba (East Algiers, Algeria) in order to remove the contained chromium. The adsorption rate has been found to be 65.70%. A comparison of kinetic models applied to the adsorption of chromium(VI) ions on the activated carbon was evaluated for the pseudo first-order, the pseudo second-order, and intraparticle diffusion kinetic models, respectively. Results show that the pseudo first-order kinetic model was found to correlate the experimental data well. In other hand, the sorption rates at different temperatures were found to increase with increasing temperature and an activation energy of approximately 9.16 x 10~(-3) kJ/mol was determined. The findings of this investigation suggested that the physical sorption was the mode controlling the sorption rate. Thermodynamic parameters were calculated. The positive value of standard enthalpy of adsorption, ΔH°_(ads), = 14.51 x 10~(-3) kJ/mol revealed the endothermic nature of the adsorption process, the positive entropy of adsorption, ΔS°_(ads) = 104.12J/molK reflected the affinity of the adsorbent material toward chromium(VI) and the negative values of Gibbs free energy, ΔG°_(ads) were indicative of the spontaneity of the adsorption process.
机译:已经研究了通过活性炭水溶液从水溶液中除去铬(VI)作为溶液pH,初始铬浓度C,固体/液体比率R和温度T,Freundlich和Langmuir模型已应用和平衡吸附被发现最适合Langmuir吸附等温线,在大多数情况下,在大多数情况下观察到铬(VI)离子的理论和实验性平衡浓度之间的良好相关性。摄取分布系数,K_D表示,去除铬(VI)以最低的固液比最高。通过使用2〜4个完整的因子设计进行经验建模,并从数据中确定吸附铬(VI)的回归方程。 pH和温度是影响铬(VI)吸附的最重要的参数,其次是固体/液体比,而初始铬(VI)浓度对该方法具有最负面影响。然而,相互作用pH-固液比温度具有阳性作用。获得的最佳参数,pH 3.62; c = 77.35 mg / l; r = 10和t = 45°C,已应用于Rouiba(东阿尔及利亚,阿尔及利亚)的制革厂的废水,以除去所含的铬。已发现吸附率为65.70%。评价应用于活性炭上的铬(VI)离子的吸附的动力学模型的比较分别用于伪第一阶,伪二阶和骨盆扩散动力学模型。结果表明,发现伪第一阶动力学模型将实验数据吻合良好。另一方面,发现不同温度下的吸附速率随着温度的增加而增加,测定约9.16×10〜(-3)kJ / mol的活化能。该研究的结果表明,物理吸附是控制吸附率的模式。计算热力学参数。标准吸附焓的正值,ΔH°_(ADS),= 14.51×10〜(-3)KJ / mol显示吸附过程的吸热性,吸附的正熵,ΔS°_(ADS)= 104.12J / Molk反映了吸附材料对铬(VI)的亲和力,并且Gibbs自由能的负值,ΔG°_(ADS)表示吸附过程的自发性。

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