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Phenol removal from aqueous solution by adsorption and ion exchange mechanisms onto polymeric resins

机译:通过吸附和离子交换机制从水溶液中除去苯酚到聚合树脂上

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摘要

The removal of phenol from aqueous solution was evaluated by using a nonfunctionalized hyper-cross-linked polymer Macronet MN200 and two ion exchange resins, Dowex XZ (strong anion exchange resin) and AuRIX 100 (weak anion exchange). Equilibrium experimental data were fitted to the Langmuir and Freundlich isotherms at different pHs. The Langmuir model describes successfully the phenol removal onto the three resins. The extent of the phenol adsorption was affected by the pH of the solution; thus, the nonfunctionalized resin reported the maximum loading adsorption under acidic conditions, where the molecular phenol form predominates. In contrast both ion exchange resins reported the maximum removal under alkaline conditions where the phenolate may be removed by a combined effect of both adsorption and ion exchange mechanisms. A theoretical model proposed in the literature was used to fit the experimental data and a double contribution was observed from the parameters obtained by the model. Kinetic experiments under different initial phenol concentrations and under the best pH conditions observed in the equilibrium experiments were performed. Two different models were used to define the controlling mechanism of the overall adsorption process: the homogeneous particle diffusion model and the shell progressive model fit the kinetic experimental data and determined the resin phase mechanism as the rate-limiting diffusion for the phenol removal. Resins charged after the kinetic experiments were further eluted by different methods. Desorption of nonfunctionalized resin was achieved by using the solution (50% v/v) of methanol/water with a recovery close to 90%. In the case of the ion exchange resins the desorption process was performed at different pHs and considering the effect of the competitive ion Cl~-. The desorption processes were controlled by the ion exchange mechanism for Dowex XZ and AuRIX 100 resins; thus, no significant effect for the addition of Cl~- under acidic conditions was observed, while under alkaline conditions the total recovery increased, specially for Dowex XZ resin.
机译:通过使用非官能化的超交联聚合物Macronet MN200和两种离子交换树脂Dowex XZ(强阴离子交换树脂)和AuRIX 100(弱阴离子交换)评估水溶液中苯酚的去除率。平衡实验数据适用于不同pH下的Langmuir和Freundlich等温线。 Langmuir模型成功地描述了在三种树脂上去除苯酚的方法。苯酚的吸附程度受溶液pH值的影响。因此,非官能化树脂在酸性条件下报告了最大的负载吸附,在酸性条件下,分子酚形式占主导。相反,两种离子交换树脂均在碱性条件下报告了最大去除率,在碱性条件下,酚盐可通过吸附和离子交换机制的共同作用而被去除。使用文献中提出的理论模型来拟合实验数据,并从该模型获得的参数中观察到双重贡献。在平衡实验中观察到的不同初始苯酚浓度和最佳pH条件下进行了动力学实验。使用两种不同的模型来定义整个吸附过程的控制机制:均相颗粒扩散模型和壳层渐进模型拟合动力学实验数据,并确定了树脂相机理作为去除苯酚的限速扩散。动力学实验后带电的树脂用不同的方法进一步洗脱。通过使用甲醇/水的溶液(50%v / v)实现非官能化树脂的解吸,回收率接近90%。对于离子交换树脂,解吸过程是在不同的pH值下进行的,并考虑了竞争离子Cl〜-的影响。解吸过程是通过离子交换机制控制Dowex XZ和AuRIX 100树脂的;因此,在酸性条件下,未观察到添加Cl-的显着影响,而在碱性条件下,总回收率增加了,特别是对于Dowex XZ树脂而言。

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