反应速率常数
动力学
废水
总有机碳
化学
降级(电信)
化学动力学
生物降解
动能
有机化合物
反应速率
速率方程
环境化学
污水处理
制浆造纸工业
化学需氧量
工业废水处理
活性炭
碳纤维
环境工程
环境科学
有机化学
催化作用
计算机科学
电信
物理
量子力学
工程类
作者
Helcio José Izário Filho,Leandro G. Aguiar,Adriano Francisco Siqueira,Marco Aurélio Kondracki de Alcântara,Patrícia Caroline Molgero Da Rós,Robson Sø Rocha,Diovana Aparecida dos Santos Napoleão,Joaquim Joffre Brandão
标识
DOI:10.1007/s11270-021-05039-w
摘要
This study aimed to investigate the degradation kinetics of the total organic carbon (TOC) in real pharmaceutical wastewater. Because of the complexity of real wastewaters and the lack of knowledge on all reactions involved in their chemical degradation, the use of a kinetic approach becomes difficult. To overcome this difficulty, we adopted a kinetic model based on chemical equations validated for mechanisms of free radical generation. Photo-Fenton reactions were performed in a 1-L tubular reactor. The developed model satisfactorily described the degradation kinetics of TOC in wastewater, with an R2 of 0.9997. The TOC degradation rate constant (kd) was estimated at 1 × 1011 L2 mol2 s−1, in agreement with literature values for the degradation kinetics of organic compounds. UV radiation had a positive effect on degradation, contributing to HO• formation. The adopted mathematical approach was highly sensitive to the formation rate constant of HO• from H2O2 (k4). By assuming the reaction to follow variable order kinetics (β = 1 and β = 2), it was possible to improve the goodness of fit of the model. Our results suggest, albeit in an incipient way, that the approach used in this study can be extended to the kinetic understanding of other complex wastewaters.
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