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Kinetic study of defluoridation of drinking water by electrocoagulation/electroflotation in a stirred tank reactor and in an external-loop airlift reactor

机译:在搅拌釜反应器和外环气提反应器中通过电凝/电浮法对饮用水进行脱氟的动力学研究

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A kinetic study of defluoridation of drinking water was carried out using the electrocoagula-tion/electroflotation process in two batch reactors of identical volume (20 L): a stirred tank reactor (STR) and an external-loop airlift reactor (ELALR). When the evolution of fluoride content was independent of stirring speed, experimental results showed that the kinetics of fluoride removal could be modelled using a variable-order-kinetic (VOK) approach coupled with a Langmuir-Freundlich adsorption model in the STR. Conversely, when mixing was less efficient, which is the case in the ELALR, experimental data could be fitted adequately only using a pseudo-first-order model. This constitutes however only an empirical approach based on a lumped parameter that accounts simultaneously for mass transfer, adsorption and electrochemical steps. In this case, only regression analysis could be used to establish a quantitative relationship between the kinetic constant and the operating conditions, such as current density and initial fluoride concentration.
机译:在两个容量相同(20升)的间歇式反应器中,采用电凝/电浮法对饮用水的脱氟进行了动力学研究:搅拌釜反应器(STR)和外环气提反应器(ELALR)。当氟化物含量的变化与搅拌速度无关时,实验结果表明,可使用STR中的Langmanir-Freundlich吸附模型与可变动力学(VOK)方法结合,对脱氟动力学进行建模。相反,当混合效率较低时(在ELALR中就是这种情况),仅使用伪一阶模型就可以充分拟合实验数据。然而,这仅构成基于集总参数的经验方法,该集总参数同时考虑了传质,吸附和电化学步骤。在这种情况下,只能使用回归分析来建立动力学常数和运行条件(例如电流密度和初始氟化物浓度)之间的定量关系。

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