Solar photocatalytic degradation of commercial textile azo dyes: Performance of pilot plant scale thin film fixed-bed reactor

Desalination ◽  
2009 ◽  
Vol 246 (1-3) ◽  
pp. 344-352 ◽  
Author(s):  
Ghanem Zayani ◽  
Latifa Bousselmi ◽  
Farouk Mhenni ◽  
Ahmed Ghrabi
Author(s):  
Fernando Martínez ◽  
M Isabel Pariente ◽  
Juan Antonio Melero ◽  
Juan Ángel Botas

AbstractCatalytic Wet Peroxide Oxidation (CWPO) for the continuous treatment of a phenolic aqueous solution has been studied on a pilot scale process. The pilot plant has been designed by integration of a catalytic fixed bed reactor (FBR) with a continuous stirred tank reactor (CSTR). The CSTR is used as reservoir for the continuous delivering of a recirculation stream through the catalytic bed. The main part of phenol mineralization takes place by catalytic oxidation in the FBR. The mesoporous SBA-15 silica-supported iron oxide (Fe


2016 ◽  
Vol 74 (7) ◽  
pp. 1680-1688 ◽  
Author(s):  
Feigao Xu ◽  
Wencheng Tan ◽  
Heng Liu ◽  
Dan Li ◽  
Yuexiang Li ◽  
...  

Crack-free PDMS-SiO2-TiO2 composite as photocatalyst was prepared for degrading dyes by using thin-film fixed bed reactor. The hydrophobic surface of the photocatalyst loaded with PDMS-SiO2-TiO2 composite could be considered as an extractant for organic pollutants. The effect of different supports including pumice stone, medicinal stone, and fiberglass for photocatalytic efficiency were compared. Under the same condition, it was found that the photocatalytic degradation effect of dyes was best when PDMS-SiO2-TiO2 composite was fixed on pumice stone rather than medicinal stone or fiberglass. Furthermore, when pumice stone was used as the support for PDMS-SiO2-TiO2 composite, the photocatalytic degradation effect of dyes hardly decreased after five cycles.


2010 ◽  
Vol 61 (7) ◽  
pp. 1829-1836 ◽  
Author(s):  
M. I. Pariente ◽  
J. A. Melero ◽  
F. Martínez ◽  
J. A. Botas ◽  
A. I. Gallego

Continuous Catalytic Wet Hydrogen Peroxide Oxidation (CWHPO) for the treatment of a petrochemical industry wastewater has been studied on a pilot plant scale process. The installation, based on a catalytic fixed bed reactor (FBR) coupled with a stirred tank reactor (STR), shows an interesting alternative for the intensification of a continuous CWHPO treatment. Agglomerated SBA-15 silica-supported iron oxide (Fe2O3/SBA-15) was used as Fenton-like catalyst. Several variables such as the temperature and hydrogen peroxide concentration, as well as the capacity of the pilot plant for the treatment of inlet polluted streams with different dilution degrees were studied. Remarkable results in terms of TOC reduction and increased biodegradability were achieved using 160°C and moderate hydrogen peroxide initial concentration. Additionally, a good stability of the catalyst was evidenced for 8 hours of treatment with low iron leaching (less than 1 mg/L) under the best operating conditions.


2010 ◽  
Vol 61 (2) ◽  
pp. 507-512 ◽  
Author(s):  
Carlos Sordo ◽  
Rafael Van Grieken ◽  
Javier Marugán ◽  
Pilar Fernández-Ibáñez

The photocatalytic disinfection efficiency has been investigated for two immobilized TiO2 catalytic systems (wall reactor and fixed-bed reactor) in a solar pilot plant. Their performances have been compared with the use of a slurry reactor and the solar disinfection without catalyst. The use of photocatalytic TiO2 wall reactors does no show clear benefits over the solar disinfection process in the absence of catalyst. The reason is that the efficiency of the solar disinfection is so high that the presence of titania in the reactor wall reduces the global efficiency due to the competition for the absorption of photons. As expected, the maximum efficiency was shown by the slurry TiO2 reactor, due to the optimum contact between bacteria and catalyst. However, it is noticeable that the use of the fixed-bed reactor leads to inactivation rate quite close to that of the slurry, requiring comparable accumulated solar energy of about 6 kJ L−1 to achieve a 6-log decrease in the concentration of viable bacteria and allowing a total disinfection of the water (below the detection limit of 1 CFU mL−1). Not only the high titania surface area of this configuration is responsible for the bacteria inactivation but the important contribution of the mechanical stress has to be considered. The main advantage of the fixed-bed TiO2 catalyst is the outstanding stability, without deactivation effects after ten reaction cycles, being readily applicable for continuous water treatment systems.


2003 ◽  
Vol 156 (1-3) ◽  
pp. 179-187 ◽  
Author(s):  
M Noorjahan ◽  
M Pratap Reddy ◽  
V Durga Kumari ◽  
B Lavédrine ◽  
P Boule ◽  
...  

2019 ◽  
Vol 10 (05) ◽  
pp. 171-184 ◽  
Author(s):  
Ignace Christian M’Bra ◽  
Grah Patrick Atheba ◽  
Didier Robert ◽  
Patrick Drogui ◽  
Albert Trokourey

2007 ◽  
Vol 129 (1-2) ◽  
pp. 59-68 ◽  
Author(s):  
Javier Marugán ◽  
Jose Aguado ◽  
Wolfgang Gernjak ◽  
Sixto Malato

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