K. (2005). Different fouling modes of submerged hollow-fiber and flat-sheet membranes induced by high strength wastewater with concurrent biofouling. Desalination, 180 (1-3), 89-97. Different fouling modes of submerged hollow-fiber and flat-sheet membranes induced by high strength wastewater with concurrent biofouling Abstract Exploration of two major commercialized flat-sheet and hollow-fiber membranes in a submerged membrane fungi reactor fed with a synthetic textile wastewater revealed striking differences in the extent and mechanism of fouling between the two types, indicating a case-specific scope of choice between the two for industrial wastewater treatment. The hollow-fiber membrane exhibited fouling with a cake layer composed of fungi and starch, intensity being proportional to the operating flux (0.05-0.3 m/d). Conversely, the flat-sheet membrane suffered from immediate internal pore blocking beyond a critical flux of 0.2 m/d. During the experiment with major constituents of the synthetic wastewater separately, while media containing only starch and only dye induced negligible fouling, flux-dependent pore blocking was evident for both the hollow-fiber (0.288 m/d) and flat-sheet membranes (1.3 m/d) for the mixture of starch and dye. Despite a remarkable 99% color and 97% TOC removal achieved by both membranes, fouling with different modes and intensity for the two types under similar conditions and for the same type of membrane under different exposure conditions warrants development of suitable modules for such recalcitrant wastewater. Tokyo, Tokyo,, Japan.
AbstractExploration of two major commercialized flat sheet and hollow fiber membranes in a submerged membrane fungi reactor fed with a synthetic textile wastewater revealed striking difference in extent and mechanism of fouling between the two types, indicating case-specific scope of choice between those for industrial wastewater treatment. The hollow fiber membrane exhibited fouling by cake-layer composed of fungi and starch, intensity being proportional to the operating flux (0.05-0.3 m/d). Conversely, the flat sheet membrane suffered from immediate internal pore-blocking beyond a critical flux of 0.2 m/d. During experiment with major constituents of the synthetic wastewater separately, while media containing only starch and only dye induced negligible fouling, flux-dependent pore-blocking emerged in case of both the hollow fiber (0.288 m/d) and flat sheet membranes (1.3 m/d) for the mixture of starch and dye. Despite a remarkable 99% color and 97% TOC removal achieved by both the membranes, fouling with different mode and intensity for the two types of membranes under similar condition, and for the same type of membrane under different exposure condition warrants development of suitable modules for such recalcitrant wastewater.