Browsing by Author "Nelson, Sara E."

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Assessing biofouling on polyamide reverse osmosis (RO) membrane surfaces in a laboratory system
(2010-04) Khan, Mohiuddin M. T.; Stewart, Philip S.; Moll, D. J.; Mickols, W. E.; Burr, Mark D.; Nelson, Sara E.; Camper, Anne K.
Biofouling of reverse osmosis (RO) membranes is a major impediment in both wastewater reuse and desalination of sea/brackish waters. A benefit to the industry would be a simple screening approach to evaluate biofouling resistant RO membranes for their propensity to biofoulants. To observe the relationship between initial membrane productivity and control of biofilm formation governed by surface modification to the aromatic polyamide thin-film composite RO membranes, three different RO membranes developed by the FilmTec Corporation including FilmTecâ€™s commercial membrane BW30 (RO#1) and two experimental membranes (RO #2 and #3) were used. RO #2 and RO #3 were modified with a proprietary aliphatic group and with an extra proprietary aromatic group, respectively. Membrane swatches were fixed on coupons in rotating disk reactor systems without filtration and exposed to water with indigenous organisms supplemented with 1.5 mg/L organic carbon under continuous flow. After biofouling had developed, the membranes were sacrificed and subjected to several analyses. Staining and epifluorescence microscopy revealed more cells on RO #2 and #3 compared to RO #1. Based on image analysis of 5-Âµmthick stained biofoulant cryo-sections, the accumulation of hydrated biofoulants on RO #1 and #3 were from 0.87 to 1.26Âµm/day, which was lower than that on RO#2 (2.19Âµm/day). Biofoulants increased the hydrophobicity of RO #2 to the greatest amount, up to 32Â°, as determined by contact angle. In addition, a wide range of changes of the chemical elements of the RO surfaces was observed with X-ray photoelectron spectroscopy analysis. RO #2 with the highest initial membrane productivity showed the poorest biofouling resistance. A combination of these novel approaches showed good agreement and suggested that membrane productivity, heterogeneity of anti-biofouling agents on membrane surface, stability of surface chemical elements and the role of virgin RO surface hydrophobicity should be jointly considered during the development of anti-biofouling polyamide thin-film RO surfaces.
Characterization and effect of biofouling on polyamide reverse osmosis and nanofiltration membrane surfaces
(2011-01) Khan, Mohiuddin M. T.; Stewart, Philip S.; Moll, D. J.; Mickols, W. E.; Nelson, Sara E.; Camper, Anne K.
Biofouling is a major reason for flux decline in the performance of membrane-based water and wastewater treatment plants. Initial biochemical characterization of biofilm formation potential and biofouling on two commercially available membrane surfaces from FilmTec Corporation were investigated without filtration in laboratory rotating disc reactor systems. These surfaces were polyamide aromatic thin-film reverse osmosis (RO) (BW30) and semi-aromatic nanofiltration (NF270) membranes. Membrane swatches were fixed on removable coupons and exposed to water with indigenous microorganisms supplemented with 1.5 mg l−1 organic carbon under continuous flow. After biofilms formed, the membrane swatches were removed for analyses. Staining and epifluorescence microscopy revealed more cells on the RO than on the NF surface. Based on image analyses of 5-μm thick cryo-sections, the accumulation of hydrated biofoulants on the RO and NF surfaces exceeded 0.74 and 0.64 μm day−1, respectively. As determined by contact angle the biofoulants increased the hydrophobicity up to 30° for RO and 4° for NF surfaces. The initial difference between virgin RO and NO hydrophobicities was ∼5°, which increased up to 25° after biofoulant formation. The initial roughness of RO and NF virgin surfaces (75.3 nm and 8.2 nm, respectively) increased to 48 nm and 39 nm after fouling. A wide range of changes of the chemical element mass percentages on membrane surfaces was observed with X-ray photoelectron spectroscopy. The initial chemical signature on the NF surface was better restored after cleaning than the RO membrane. All the data suggest that the semi-aromatic NF surface was more biofilm resistant than the aromatic RO surface. The morphology of the biofilm and the location of active and dead cell zones could be related to the membrane surface properties and general biofouling accumulation was associated with changes in the surface chemistry of the membranes, suggesting the validity of the combination of these novel approaches for initial assessment of membrane performance.
Combined effects of EPS and HRT enhanced biofouling on a submerged and hybrid PAC-MF membrane bioreactor
(2013-02) Khan, Mohiuddin M. T.; Takizawa, S.; Lewandowski, Zbigniew; Rahman, M. Habibur; Komatsu, K.; Nelson, Sara E.; Kurisu, F.; Camper, Anne K.; Katayama, H.; Ohgaki, S.
The goal of this study was to quantify and demonstrate the dynamic effects of hydraulic retention time (HRT), organic carbon and various components of extracellular polymeric substances (EPS) produced by microorganisms on the performance of submersed hollowfiber microfiltration (MF) membrane in a hybrid powdered activated carbon (PAC)-MF membrane bioreactor (MBR). The reactors were operated continuously for 45 days to treat surface (river) water before and after pretreatment using a biofiltration unit. The real-time levels of organic carbon and the major components of EPS including five different carbohydrates (D(Ã¾) glucose and D(Ã¾) mannose, D(Ã¾) galactose, N-acetyl-D-galactosamine and Dgalactose, oligosaccharides and L( ) fucose), proteins, and polysaccharides were quantified in the influent water, foulants, and in the bulk phases of different reactors. The presence of PAC extended the filtration cycle and enhanced the organic carbon adsorption and removal more than two fold. Biological filtration improved the filtrate quality and decreased membrane fouling. However, HRT influenced the length of the filtration cycle and had less effect on organic carbon and EPS component removal and/or biodegradation. The abundance of carbohydrates in the foulants on MF surfaces was more than 40 times higher than in the bulk phase, which demonstrates that the accumulation of carbohydrates on membrane surfaces contributed to the increase in transmembrane pressure significantly and PAC was not a potential adsorbent of carbohydrates. The abundance of N-acetyl-Dgalactosamine and D-galactose was the highest in the foulants on membranes receiving biofilter-treated river water. Most of the biological fouling compounds were producedinside the reactors due to biodegradation. PAC inside the reactor enhanced the biodegradation of polysaccharides up to 97% and that of proteins by more than 95%. This real-time extensive and novel study demonstrates that the PAC-MF hybrid MBR is a sustainable technology for treating river water.
Enzymatic cleaning of biofouled thin-film composite reverse osmosis (RO) membrane operated in a biofilm membrane reactor
(2014-06) Khan, Mohiuddin M. T.; Danielsen, S.; Johansen, K.; Nelson, Sara E.; Camper, Anne K.
Application of environmentally friendly enzymes to remove thin-film composite (TFC) reverse osmosis (RO) membrane biofoulants without changing the physico-chemical properties of the RO surface is a challenging and new concept. Eight enzymes from Novozyme A/S were tested using a commercially available biofouling-resistant TFC polyamide RO membrane (BW30, FilmTech Corporation, Dow Chemical Co.) without filtration in a rotating disk reactor system operated for 58 days. At the end of the operation, the accumulated biofoulants on the TFC RO surfaces were treated with the three best enzymes, Subtilisin protease and lipase; dextranase; and polygalacturonase (PG) based enzymes, at neutral pH (~7) and doses of 50, 100, and 150 ppm. Contact times were 18 and 36 h. Live/dead staining, epifluorescence microscopy measurements, and 5 Âµm thick cryo-sections of enzyme and physically treated biofouled membranes revealed that Subtilisin protease- and lipase-based enzymes at 100 ppm and 18 h contact time were optimal for removing most of the cells and proteins from the RO surface. Culturable cells inside the biofilm declined by more than five logs even at the lower dose (50 ppm) and shorter incubation period (18 h). Subtilisin protease- and lipase-based enzyme cleaning at 100 ppm and for 18 h contact time restored the hydrophobicity of the TFC RO surface to its virgin condition while physical cleaning alone resulted in a 50Â° increase in hydrophobicity. Moreover, at this optimum working condition, the Subtilisin protease- and lipase-based enzyme treatment of biofouled RO surface also restored the surface roughness measured with atomic force microscopy and the mass percentage of the chemical compositions on the TFC surface estimated with X-ray photoelectron spectroscopy to its virgin condition. This novel study will encourage the further development and application of enzymes to remove biofoulants on the RO surface without changing its surface properties.