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Beilstein J. Nanotechnol. 2015, 6, 2423–2430, doi:10.3762/bjnano.6.250
Figure 1: Schematic of the experimental setup consisting of a reservoir, pump, photoreactor and irradiator.
Figure 2: The photoreactor placed in front of the irradiator and the UV intensity distribution on the illumin...
Figure 3: Apparent reaction rate constant K for the whole system and the intrinsic reaction rate constant k i...
Figure 4: Aggregate size of P25 as a function of ultrasonic energy density performed by two ultrasonic device...
Figure 5: (a) Light transmittance (T) through a 1 cm optical path length and (b) extinction coefficient (ε) o...
Figure 6: Dependence of MB discoloration in 1 g/L P25 suspensions on the photocatalyst aggregate size achieve...
Figure 7: Influence of P25 catalyst concentration on the reaction rate constant and the transmittance through...
Beilstein J. Nanotechnol. 2014, 5, 476–484, doi:10.3762/bjnano.5.55
Figure 1: General pre-treatment steps prior to membrane separation.
Figure 2: Photocatalysis as the master process responsible for the reduction of organic and fouling matter wi...
Figure 3: Nanofiltration as the master process responsible for the major reduction of colour and organic comp...
Figure 4: Photocatalysis combined with a submerged UF separation and a down-stream NF and RO treatment.
Figure 5: Specific equipment cost (SEC) per m2 of membrane area.
Figure 6: Total specific treatment costs of dye industry effluent versus the operating time in d/a with a mea...
Figure 7: Specific total operating costs, treatment capacity 20 m3/d and 100 m3/d, 365 days per year treatmen...