Gabriel N de O Teixeira, Arthur M S da Cruz, G. L. Samanamud, A. B. França, L. Naves, Diego Melo, Daiana Morais, E. P. Baston, F. Naves
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引用次数: 2
Abstract
Abstract The main objective of this study is the degradation of a synthetic solution of atrazine by a modified vermiculite catalyzed ozonation, in a rotating packed bed (RPB) reactor. A 0.5 L RPB reactor was used to perform the experiments, using a Central Composite Design (CCD) response surface to construct the quadratic model based on the factors: pH, catalyst concentration and reactor rotation frequency. The response variable was the removal of the organic load measured in terms of Chemical Oxygen Demand (COD). After the complete quadratic model was constructed through the response surface, the COD degradation process had an optimal removal of 41% under the following conditions: pH 8.0, rotation of 1150 rpm and catalyst concentration 0.66 g L−1.
摘要本研究的主要目的是在旋转填充床(RPB)反应器中采用改性蛭石催化臭氧氧化法降解阿特拉津合成溶液。采用0.5 L RPB反应器进行实验,采用中心复合设计(CCD)响应面建立了以pH、催化剂浓度和反应器旋转频率为影响因素的二次元模型。响应变量为以化学需氧量(COD)衡量的有机负荷去除量。通过响应面构建完整的二次元模型后,在pH 8.0、转速1150 rpm、催化剂浓度0.66 g L−1条件下,COD的最佳去除率为41%。