Graphical abstractBilge water degradation and separation via hybrid photocatalytic membrane reactor based on polyvinylidene fluoride (PVDF)/halloysite nanotube clay (HNTs) nanocomposite membrane has been achieved by this study.
AbstractThis study focuses on the design and performance of a hybrid system consisting of a photocatalytic reactor and ultrafiltration permeation cell. Initially, an ultraviolet (UV) lamp was installed in the photocatalytic reactor to decompose the bilge organic pollutants in the presence of 200 ppm titanium-dioxide (TiO 2 ). Individual hydrocarbon compounds of bilge water samples were identified by gas chromatography-mass spectrometry (GC-MS) analysis.Two types of membrane, which are pure polyvinylidene fluoride (PVDF) membrane and PVDF/modified halloysite nanotube clay (M-HNTs) nanocomposite membrane was fabricated aiming to enhance the rejection, flux and fouling resistance for full filtration of pollutants from photocatalytic reactor. Membranes were characterized by Fourier transform infrared (FTIR), field emission scanning electron microscopy (FESEM) and atomic force microscopy (AFM). Furthermore, GC-MS analysis showed that, over 90% bilge decomposition occurred by photocatalytic reaction. The TiO 2 cross-over during permeation was detected by using atomic absorption spectrophotometer (AAS), which proved that, TiO 2 rejection was more than 99% for nanocomposite membrane. UV−vis spectrophotometer confirmed over 99% rejection of decomposed bilge hydrocarbon via nanocomposite membrane with 1.0 wt.% of M-HNTs incorporated in PVDF matrix.where J p,t was the flux at time t (Lm -2 h -1 ), and J p,i was the initial flux (Lm -2 h -1 ). Flux recovery has been caculated by the Eq. (4) 51 : w2 FR w1 J R 100 J
Eq. (4) where J w2 was the flux at second time t (Lm -2 h -1 ) after membrane back washing, typically t is equal to 1 h, and J w1 was the flux at first time (Lm -2 h -1 ), at typically t equal to 1 h.