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Electrochemical regeneration of granular activated carbon saturated with Rhodamine B in a fluidized electrochemical reactor

机译:在流化电化学反应器中用若丹明B饱和的粒状活性炭的电化学再生

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摘要

This study investigated the electrochemical regeneration in fluidized reactor, used for granular activated carbon (GAC) saturated with Rhodamine B (RB). The regeneration efficiency is mainly affected by the generation of active spices including hydroxyl radicals. In this present modified study, the improvement of mass transfer using fluidized reactor lead to increase regeneration efficiency. This process was modelled and optimized using response surface methodology (RSM) based on central composite design (CCD). Such effective parameters on regeneration efficiency (RE) as current density, regeneration time and electrolyte flow rate were optimized and modelled using reduced quadratic model. The predictive ability of proposed model was verified by computing correlation coefficient (R-2 = 0.9956). At optimum condition, effective parameters of current density = 3.79 (mA cm(-2)), regeneration time = 100 (min) and electrolyte flow rate = 274.5 (mL min(-1)), maximum regeneration efficiency (83.7%) was achieved. The results of which were obtained after four time sequential adsorption-desorption cycles were acceptable. In conclusion, the modified electrochemical regeneration method is suggested to be used more widely as cost-effective technique.
机译:这项研究调查了流化反应器中的电化学再生,该反应器用于用若丹明B(RB)饱和的颗粒状活性炭(GAC)。再生效率主要受包括羟基自由基在内的活性香料产生的影响。在本修改研究中,使用流化反应器的传质改进导致再生效率的提高。使用基于中央复合设计(CCD)的响应面方法(RSM)对这一过程进行建模和优化。诸如电流密度,再生时间和电解液流速之类的关于再生效率(RE)的有效参数被优化并使用简化的二次模型进行建模。通过计算相关系数(R-2 = 0.9956),验证了所提模型的预测能力。在最佳条件下,有效参数的电流密度= 3.79(mA cm(-2)),再生时间= 100(min)和电解液流速= 274.5(mL min(-1)),最大再生效率为(83.7%)。实现。在四个连续的吸附-解吸循环后获得的结果是可以接受的。总之,改进的电化学再生方法被认为是更经济有效的技术。

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