Xiufen Li

Impacts of sludge retention time on sludge characteristics and membrane fouling in a submerged osmotic membrane bioreactor.

Sludge retention time (SRT) is a feasible method to alleviate the salt accumulation in the osmotic membrane bioreactor (OMBR) by discharging the waste activated sludge. In this study, effects of SRT on sludge characteristics and membrane fouling were investigated using a submerged OMBR under two SRTs of 10 and 15d. The results showed that the lower SRT was helpful for alleviating the salt accumulation and flux decline. Besides that, the removal of NH3-N was significantly influenced by SRT. SRT also had a strong effect on soluble microbial products (SMP) and microbial activity due to the variation of salinity. Microbial diversity analysis indicated that the high salinity environment in the OMBR significantly affected the microbial communities. The flux decline in the OMBR was mainly attributed to the reduced driving force resulting from the salt accumulation, and the reversible fouling was the dominant forward osmosis (FO) membrane fouling in the OMBR.

Integration of micro-filtration into osmotic membrane bioreactors to prevent salinity build-up.

The high salinity remains as one of major obstacles of the osmotic membrane bioreactor (OMBR). In this study, a new pathway was explored to prevent the salinity build-up by integrating the micro-filtration (MF) membrane to the OMBR (MF-OMBR). The results indicated that the salinity characterized by conductivity in the MF-OMBR was effectively alleviated and controlled at a lower value of about 5 mS/cm, and the stable flux of forward osmosis (FO) membrane correspondingly increased to approximately 5.5L/(m(2)h). Besides, the addition of MF membrane in the OMBR could increase the total organic carbon (TOC) and ammonium nitrogen (NH3-N) removals due to the activated sludge by improving the microbial activity. The membrane fouling especially the reversible fouling in the MF-OMBR was severer compared to that in the conventional OMBR, which resulted in a lower water flux than the expectation due to the increase of filtration resistance and external concentration polarization.

In situ observation of the growth of biofouling layer in osmotic membrane bioreactors by multiple fluorescence labeling and confocal laser scanning microscopy.

Since the concept of the osmotic membrane bioreactor (OMBR) was introduced in 2008, it has attracted growing interests for its potential applications in wastewater treatment and reclamation; however, the fouling mechanisms of forward osmosis (FO) membrane especially the development of biofouling layer in the OMBR are not yet clear. Here, the fouled FO membranes were obtained from the OMBRs on days 3, 8 and 25 in sequence, and then the structure and growing rule of the biofouling layer formed on the FO membrane samples were in-situ characterized by multiple fluorescence labeling and confocal laser scanning microscopy (CLSM). CLSM images indicated that the variations in abundance and distribution of polysaccharides, proteins and microorganisms in the biofouling layer during the operation of OMBRs were significantly different. Before the 8th day, their biovolume dramatically increased. Subsequently, the biovolumes of β-d-glucopyranose polysaccharides and proteins continued increasing and leveled off after 8 days, respectively, while the biovolumes of α-d-glucopyranose polysaccharides and microorganisms decreased. Extracellular polymeric substances (EPS) played a significant role in the formation and growth of biofouling layer, while the microorganisms were seldom detected on the upper fouling layer after 3 days. Based on the results obtained in this study, the growth of biofouling layer on the FO membrane surface in the OMBR could be divided into three stages. Initially, EPS was firstly deposited on the FO membrane surface, and then microorganisms associated with EPS located in the initial depositing layer to form clusters. After that, the dramatic increase of the clusters of EPS and microorganisms resulted in the quick growth of biofouling layer during the flux decline of the OMBR. However, when the water flux became stable in the OMBR, some microorganisms and EPS would be detached from the FO membrane surface.

Comparison of biofouling mechanisms between cellulose triacetate (CTA) and thin-film composite (TFC) polyamide forward osmosis membranes in osmotic membrane bioreactors

There are two types of popular forward osmosis (FO) membrane materials applied for researches on FO process, cellulose triacetate (CTA) and thin film composite (TFC) polyamide. However, performance and fouling mechanisms of commercial TFC FO membrane in osmotic membrane bioreactors (OMBRs) are still unknown. In current study, its biofouling behaviors in OMBRs were investigated and further compared to the CTA FO membrane. The results indicated that β-D-glucopyranose polysaccharides and microorganisms accounted for approximately 77% of total biovolume on the CTA FO membrane while β-D-glucopyranose polysaccharides (biovolume ratio of 81.1%) were the only dominant biofoulants on the TFC FO membrane. The analyses on the biofouling structure implied that a tighter biofouling layer with a larger biovolume was formed on the CTA FO membrane. The differences in biofouling behaviors including biofoulants composition and biofouling structure between CTA and TFC FO membranes were attributed to different membrane surface properties.

Typical methanogenic inhibitors can considerably alter bacterial populations and affect the interaction between fatty acid degraders and homoacetogens

The effects of two typical methanogenic inhibitors [2-bromoethanesulfonate (BES) and chloroform (CHCl3)] on the bacterial populations were investigated using molecular ecological techniques. Terminal restriction fragment length polymorphism analyses (T-RFLP) in combination with clone library showed that both the toxicants not only inhibited methanogenic activity but also considerably altered the bacterial community structure. Species of low % G + C Gram-positive bacteria (Clostridiales), high % G + C Actinomycetes, and uncultured Chloroflexi showed relatively greater tolerance of CHCl3, whereas the BES T-RFLP patterns were characterized by prevalence of Geobacter hydrogenophilus and homoacetogenic Moorella sp. In addition, due to indirect thermodynamic inhibition caused by high hydrogen partial pressures, the growth of obligately syntrophic acetogenic Syntrophomonas and Syntrophobacter was also affected by selective inhibition of methanogenesis. Interestingly, by comparing the fermentative intermediates detected in BES- and CHCl3-treated experiments, it was furthermore found that when methanogenesis is specifically inhibited, the syntrophic interaction between hydrogen-producing fatty acid degraders and hydrogen-utilizating homoacetogens seemed to be strengthened.

Characterization and fouling properties of exopolysaccharide produced by Klebsiella oxytoca

Klebsiella oxytoca produced a type of exopolysaccharide (EPS) with the average molecular weight (Mw) of 116,018 Da and the average size of 260 nm. The EPS monosaccharide components contained rhamnose, fucose, arabinose, xylose, mannose, galactose and glucose and the molar ratio among them was 0.033:0.0411:0.0147:0.0051:0.2393:0.0986:0.1304. Typical EPS absorption peaks in FT-IR spectrum and pseudoplastic properties were also revealed. The polyvinylidenefluoride (PVDF) membrane showed a relatively larger flux decline resulted from the EPS fouling. The EPS filtration was dominated by more than one mechanism at the beginning phase and mainly by the cake formation at the later phase for both membranes. The pore blocking resistance had a predominant contribution to the filtration resistance and the cake resistance played a secondary role for both the membranes. The EPS adsorption resulted in a weak membrane fouling. The PVDF membrane exhibited a larger adsorption resistance than the polypropylene (PP) membrane.

A monolithic three-dimensional macroporous graphene anode with low cost for high performance microbial fuel cells

Microbial fuel cells (MFCs), capable of simultaneously degrading substrates and producing bioelectricity, have drawn great attention. However, low power output and high cost have severely hindered their practical application. The present study prepared a monolithic three-dimensional graphene (3D-G) electrode through a self-assembly method. The as-prepared 3D-G electrode featured inflexibility, a crumpled surface, a macroporous structure (with pore spaces of dozens of microns), high specific surface area (188.32 m2 g−1), good conductivity and low cost, favoring high bacterial loading capacity and enhancing the extracellular electron transfer (EET) efficiency. Equipped with the prepared 3D-G anode in an air-cathode single chamber MFC reactor, the maximum power density (Pmax) increased to 1516 ± 87 mW m−2 in the 3D-G reactor from 877 ± 57 mW m−2 in the graphite felt (GF) control and from 584 ± 39 mW m−2 in the carbon cloth (CC) control after 2 weeks of operation. Moreover, the Pmax of the reactor with the 3D-G anode decreased only by 15% after 2 months of operation, which showed durability of the anode due to having macropores which are not easily blocked. Normalized to the cost of the anode, the Pmax in the 3D-G reactor was 93 and 133 times those in the GF and CC reactors, respectively. Dynamic analysis results (CV, Tafel and EIS) showed that the 3D-G anode improved the efficiency of EET due to having an appropriate structure and good conductivity. The 3D-G anode, with superior performance and low cost, would powerfully promote the practical and large-scale application of MFCs.

Surface interactions and fouling properties of Micrococcus luteus with microfiltration membranes.

This study was conducted to investigate microbial adhesion of Micrococcus luteus to polypropylene (PP) and polyvinylidene fluoride (PVDF) membranes in relation to the variation of the interfacial energies in the membrane–bacteria systems, for revealing effects of short-range surface interactions on filtration behavior. Both the membranes and M. luteus showed typical strong electron donors and hydrophilic properties. The AB component was dominant in the interfacial energies of the two membrane–bacteria systems. M. luteus presented larger negative

Effect of short-term alkaline intervention on the performance of buffer-free single-chamber microbial fuel cell

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