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Removal of gentian violet in aqueous solution by activated carbon equilibrium, kinetics, and thermodynamic study

机译:通过活性炭均衡,动力学和热力学研究去除龙胆紫中的龙胆紫

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The quantitative kinetic and equilibrium adsorption parameters for chlorure de methylrosaniline (gentian violet, crystal violet) removed by commercial activated carbon were studied by UV-visible spectroscopy.Activated carbon with a high specific surface area 1250 m(2)/g was characterized by the Brunauer, Emmett et Teller (BET) method and the zero charge point pH ((pzc)). The adsorption properties of both activated carbon with gentian violet were conducted at variable stirring speed 100-700 trs/min, adsorbent dose 1-8 g/l, solution pH 1-14, initial gentian violet concentration 5-15 mg/l, contact time 0-50 min, and temperature 299-323 K using batch mode operation to find the optimal conditions for a maximum adsorption. The adsorption mechanism of gentian violet was studied using the pseudo-first-order, pseudo-second-order, and Elovich kinetic models. The adsorption kinetics was found to follow a pseudo-second-order kinetic model with a determination coefficient (R-2) of 0.999. The Weber-Morris diffusion model was applied for the adsorption mechanism. The equilibrium adsorption data of gentian violet were analyzed by the Langmuir, Freundlich, Elovich, and Temkin models. The results indicate that the Langmuir model provides the best correlation (q(max) = 22.727, 32.258 mg/g at 26 and 40 degrees C, respectively). The adsorption isotherms at different temperatures have been used for the determination of thermodynamic parameters, i.e. free energy (Delta G degrees = - 2.30 to -5.34 kJ/mol), enthalpy (Delta H degrees = 36.966 kJ/mol), entropy (Delta S degrees = 0.131 kJ/mol K), and activation energy (Ea) 40.208 kJ/mol of gentian violet adsorption. The negative Delta G degrees and positive Delta H degrees indicate that the overall adsorption is spontaneous and endothermic in nature.
机译:通过UV可见光谱除去商业活性炭氯胺(龙料紫,晶紫)的定量动力学和平衡吸附参数。用高比表面积1250μm(2)/ g的递增碳,其特征在于Brunauer,Emmett Et Teller(Bet)方法和零充电点pH((PZC))。在恒温紫罗兰中,在可变搅拌速度100-700 Trs / min,吸附剂量1-8g / L,溶液pH 1-14,初始龙胆紫浓度5-15 mg / L,接触,接触0-50分钟,温度299-323 k使用批量模式操作找到最大吸附的最佳条件。使用伪第一订单,伪二阶和elovich动力学模型研究了龙胆紫罗兰的吸附机制。发现吸附动力学跟随具有0.999的确定系数(R-2)的伪二阶动力学模型。韦伯 - 莫里斯扩散模型用于吸附机制。 Langmuir,Freundlich,Elovich和Temkin Models分析了龙胆紫罗兰的平衡吸附数据。结果表明,Langmuir模型提供了最佳相关性(Q(最多)= 22.727,32.258mg / g分别为26和40摄氏度)。不同温度下的吸附等温线已被用于测定热力学参数,即自由能(Delta G度= -2.30至-5.34 kJ / mol),焓(ΔH度= 36.966 kJ / mol),熵(ΔS学位= 0.131 kJ / mol k),激活能量(EA)40.208 KJ /摩尔紫罗兰吸附。负ΔG度和正δH度表明整体吸附是自然的自发性和吸热。

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