On the optimization of activated carbon-supported iron catalysts in catalytic wet peroxide oxidation process

2016 ◽  
Vol 181 ◽  
pp. 249-259 ◽  
Author(s):  
A. Rey ◽  
A.B. Hungria ◽  
C.J. Duran-Valle ◽  
M. Faraldos ◽  
A. Bahamonde ◽  
...  
2018 ◽  
Vol 6 (5) ◽  
pp. 6444-6450 ◽  
Author(s):  
Ismael F. Mena ◽  
Elena Diaz ◽  
Ivan Moreno-Andrade ◽  
Juan J. Rodriguez ◽  
Angel F. Mohedano

2014 ◽  
Vol 17 (1) ◽  
Author(s):  
Peng Liu ◽  
Chaolin Li ◽  
Qi Han ◽  
Gang Lu ◽  
Xiaoqing Dong ◽  
...  

AbstractIn this study, degradation of phenol solution by the ultraviolet-enhanced catalytic wet peroxide oxidation process (UV-CWPO) were evaluated via COD removal. Six kinds of homogeneous catalysts (Fe


2016 ◽  
Vol 91 (11) ◽  
pp. 2882-2887 ◽  
Author(s):  
Macarena Munoz ◽  
Carmen M Domínguez ◽  
Zahara M de Pedro ◽  
Asunción Quintanilla ◽  
Jose A Casas ◽  
...  

2021 ◽  
Vol 361 ◽  
pp. 30-36 ◽  
Author(s):  
J. Carbajo ◽  
A. Quintanilla ◽  
A.L. Garcia-Costa ◽  
J. González-Julián ◽  
M. Belmonte ◽  
...  

2007 ◽  
Vol 55 (1-2) ◽  
pp. 407-415 ◽  
Author(s):  
D.-K. Lee ◽  
S.-C. Kim ◽  
J.-H. Yoon

A catalytic wet peroxide oxidation process was combined with the aerated constructed wetland in order to treat the raw dyehouse wastewater to in acceptable level for reuse as washing process water. More than 90% of BOD and CODs could be removed with the wet peroxide oxidation reactor and the remaining pollutants in the treated water were transformed into biodegradable ones which could have been successfully treated at the following aerated constructed wetland. The highest values of BOD5, CODMn, CODCr, SS and T-N in the treated water were 1.6, 1.8, 2.1, 0.5 and 12.8 mg/L, respectively. These values were low enough for the treated water to be reused at the washing process.


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