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首页> 外文期刊>Chemical engineering journal >Treatment of simulated industrial wastewater by photo-Fenton process. Part I: The optimization of process parameters using design of experiments (DOE)
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Treatment of simulated industrial wastewater by photo-Fenton process. Part I: The optimization of process parameters using design of experiments (DOE)

机译:用光芬顿法处理模拟工业废水。第一部分:使用实验设计(DOE)优化过程参数

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摘要

The study reported the application of the photo-Fenton process for the treatment of simulated industrial wastewater upon pretreatment by the dark-Fenton process. The process efficiency which depends on several important process parameters such as initial pH, iron catalyst and oxidant concentration, and the UV irradiation type, was investigated. To consider the combined effects of studied process parameters, three-factor three-level Box-Behnken experimental design combined with response surface modeling was applied. The quadratic models predicting the mineralization of simulated industrial wastewater by the applied photo-Fenton processes were developed. ANOVA was applied to evaluate the significance of models and models' components. The obtained results indicated that both models can be characterized as highly accurate and predictive for the mineralization of simulated industrial wastewater. Our results show that both photo-Fenton processes can be successfully applied for the treatment of the studied simulated industrial wastewater. The presence of oxalates in simulated industrial wastewater strongly influenced the conditions for the maximal efficiency of applied photo-Fenton processes regarding the type of UV irradiation. The optimal conditions were determined to be: initial pH 3.88, [Fe~(2+)] = 5.01 mM (along with [Fe~(3+)] = 8.0 mM) and [H2O2] = 30 mM in the case of photo-Fenton process operated with UV-C irradiation; and pH 1.9, [Fe~(2+)] = 8.39 mM (along with (Fe~(3+)] = 8.0 mM) and [H2O2] = 30mM in the case of UV-A light application. The "pseudo"-second order mineralization kinetic of simulated industrial wastewater was determined in both cases with the calculated rate constants at determined optimal conditions: k1_(obs) = 12.94 x 10~(-2) M~(-1) s~(-1) and k2_(obs) = 9.71 x 10~(-2) M~(-1) s~(-1) for UV-C/Fe/H2O2 and UV-A/Fe/H2O2 processes, respectively.
机译:该研究报道了光芬顿法在暗芬顿法预处理后在模拟工业废水处理中的应用。研究了取决于几个重要工艺参数(例如初始pH,铁催化剂和氧化剂浓度以及紫外线照射类型)的工艺效率。为了考虑所研究工艺参数的综合影响,采用了三因素三级Box-Behnken实验设计与响应面建模相结合的方法。建立了通过应用光芬顿法预测模拟工业废水矿化的二次模型。应用方差分析评估模型和模型组成部分的重要性。获得的结果表明,两个模型都可以被表征为对模拟工业废水的矿化具有高度的准确性和可预测性。我们的结果表明,两种光芬顿工艺都可以成功地用于研究模拟工业废水的处理。在模拟工业废水中草酸盐的存在极大地影响了有关紫外线照射类型的光芬顿工艺最大效率的应用条件。确定最佳条件为:初始pH 3.88,[Fe〜(2+)] = 5.01 mM(以及[Fe〜(3+)] = 8.0 mM)和[H2O2] = 30 mM(在照片中) -Fenton工艺在UV-C照射下运行;在pH值为1.9的情况下,在使用UV-A光的情况下,[Fe〜(2+)] = 8.39 mM(以及(Fe〜(3+)] = 8.0 mM)和[H2O2] = 30mM。在两种情况下,在确定的最佳条件下,通过计算的速率常数确定模拟工业废水的二阶矿化动力学:k1_(obs)= 12.94 x 10〜(-2)M〜(-1)s〜(-1)和对于UV-C / Fe / H2O2和UV-A / Fe / H2O2工艺,k2_(obs)= 9.71 x 10〜(-2)M〜(-1)s〜(-1)。

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