Browsing by Author "Khan, Mohiuddin M. T."

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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.
Continuous and efficient removal of THMs from river water using MF membrane combined with high dose of PAC
(2009-12) Khan, Mohiuddin M. T.; Lewandowski, Zbigniew; Takizawa, S.; Yanade, Kyosuke; Katayama, H.; Ohgaki, S.
A combination of microfiltration (MF) membrane with a high concentration (40 g/L of the reactor) of powdered activated carbon (PAC) efficiently and continuously removed trihalomethanes (THMs) and total organic carbon (TOC) from river water for a period of two months. Without PAC, the membrane reactor was able to remove less than 18% of THMs and less than 5% of TOC; with PAC, 65 to 95% of THMs and TOC were removed. Even though the THMs concentration in the influent was steadily increasing (reaching 50 Î¼g/L), THMs concentration in the effluents from the reactors with PAC were consistently below 15 Î¼g/L. While the MF membranes alone could not remove organics, PAC and microbial activity in the biofilm deposited on the PAC particles assured long term and continuous removal of THMs. No additional PAC was added into or removed from the reactors during the filtration period. Operational parameters such as the backwashing of the membrane, interval of the filtration cycle and biological pretreatment of the river water had a small effect on the extent of THMs removal, but they increased the filtration time prior to membrane cleaning and improved the overall performance of the reactors.
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.
Membrane fouling due to dynamic particle size changes in the aerated hybrid PAC–MF system
(2011-04) Khan, Mohiuddin M. T.; Takizawa, S.; Lewandowski, Zbigniew; Jones, Warren L.; Camper, Anne K.; Katayama, H.; Ohgaki, S.
To quantify the effect of dynamic particle size changes and degradation and accumulation of suspended solids (SS) in influents to reactors on membrane fouling frequency in hybrid powder-activated carbon (PAC)–microfiltration (MF) reactors, we operated a PAC–MF system (hollow-fiber module) for more than five months to purify river water before and after pretreatment by a biofilter. The transmembrane pressure, backwashing pressure, resistance to filtration, and SS accumulation and degradation during these dynamic changes were evaluated. The initial dose of PAC was 40 g/L of the reactor and no additional PAC was added during this continuous operational period. The presence of PAC reduced the membrane resistance to filtration even at the end of filtration period when the number of particles in the smallest range (>1.0–3.6 μm) was the highest measured by the flow cytometer and microscopy image analysis. This resistance was reduced further when the river water was biofiltered prior to membrane filtration. This real-time study demonstrates that over time PAC and other particles coming into the reactors through the influents degrade and/or become smaller because of the turbulence caused by continuous aeration below the MF membrane fibers. The number of particles in the reactors with diameters less than 10 μm increased with time, increasing the fouling frequency; however, the presence of PAC further reduced the particle enhanced fouling. The presence of PAC also increased SS degradation by up to 10%. The increased number of bacteria inside the PAC–MF systems did not contribute to the number of membrane fouling. Even though the particle sizes inside the reactors became smaller with time, the gradual increase in net accumulation of SS was also an important factor controlling the performance of the PAC–MF system.
Powdered activated carbon and biofiltration improve MF performance: Part I
(2007-05) Khan, Mohiuddin M. T.; Jones, Warren L.; Camper, Anne K.; Takizawa, S.; Katayama, H.; Kurisu, F.; Ohgaki, S.
This article shows how the use of high-dose powdered activated carbon and biofiltration are able to improve the performance of membrane-based microfiltration systems. The first part, which appears here, provides an overview of the study, materials and methods, and experimental design and operational conditions of the reactors.
Specific and rapid enumeration of viable but non-culturable and viable-culturable gram-negative bacteria using flow cytometry
(2010-06) Khan, Mohiuddin M. T.; Pyle, Barry H.; Camper, Anne K.
An issue of critical concern in microbiology is the ability to detect viable but non-culturable (VBNC) and viable-culturable (VC) cells by methods other than existing approaches. Culture methods are selective and underestimate the real population and other options (direct viable count and double-staining method using epifluorescence microscopy and inhibitory substance influenced molecular methods) are also biased and time consuming. A rapid approach that reduces selectivity, decreases bias from sample storage and incubation, and reduces assay time is needed. Flow cytometry is a sensitive analytical technique that can rapidly monitor physiological states of bacteria. This report outlines a method to optimize staining protocols and the flow cytometer (FCM) instrument settings for the enumeration of VBNC and VC bacterial cells within 70 min. Experiments were performed using the FCM to quantify VBNC and VC Escherichia coli O157:H7, Pseudomonas aeruginosa, Pseudomonas syringae, and Salmonella typhimurium after staining with different fluorescent probes: SYTO 9, SYTO 13, SYTO 17, SYTO 40 and propidium iodide (PI). The FCM data were compared with specific standard nutrient agar to enumerate the number of cells in different states. By comparing results from cultures at late log phase, 1 to 64% of cells were non-culturable, 40 to 98% were culturable, and 0.7 to 4.5% had damaged cell-membranes and were therefore theoretically dead. Data obtained using four different gram-negative bacteria exposed to heat and stained with PI also illustrates the usefulness of the approach for the rapid and unbiased detection of dead vs. live organisms.