Pharmaceutical wastewater treatment using granular activated carbon and UV/H2O2 processes: Experimental analysis and modelling

被引:10
|
作者
Ghafoori, Samira [1 ]
Shah, Kiran K. [1 ]
Mehrvar, Mehrab [1 ]
Chan, Philip K. [1 ]
机构
[1] Ryerson Univ, Dept Chem Engn, Toronto, ON M5B 2K3, Canada
来源
基金
加拿大自然科学与工程研究理事会;
关键词
pharmaceutical wastewater; adsorption; UV; H2O2; total organic carbon; combined processes; P-AMINOPHENOL DEGRADATION; FENTON-LIKE DEGRADATION; RATE CONSTANTS; KINETIC-MODEL; OPTIMIZATION; OXIDATION; COMBINATION; OZONATION; RADICALS;
D O I
10.1002/cjce.21981
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The treatment of a synthetic pharmaceutical wastewater was studied using granular activated carbon (GAC) adsorption, UV/H2O2 process, and their combination. Experimental results reveal that GAC adsorption alone has 79% efficiency in total organic carbon (TOC) removal in 10min breakthrough time with the dosage of 333.33mgactivated carbon/L. The adsorption data are fitted well with the Langmuir adsorption isotherm. The UV/H2O2 process alone at 6h hydraulic retention time with optimum dosage of 4.25mgH2O2/mgCOD shows 29 and 26% TOC reduction using 185 and 254nm UV lamps, respectively. The kinetic modelling of the UV254/H2O2 process is developed using chemical oxygen demand (COD) and TOC as lumped parameters. A good agreement between model predictions and experimental data is confirmed. In combined processes, pre-treated pharmaceutical wastewater by UV254/H2O2 followed by GAC adsorption process along with the desorption of contaminants from GAC and the subsequent treatment of the condensed steam by UV254/H2O2 process leads to 82 % TOC removal efficiency. On the other hand, the GAC adsorption along with UV254/H2O2 treatment of regenerant (condensed steam) from the desorption process leads to 88 % TOC removal at optimum conditions.
引用
收藏
页码:1163 / 1173
页数:11
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