Characterization of membrane foulants in a pilot-scale powdered activated carbon–membrane bioreactor for drinking water treatment

The external and internal foulants of a pilot-scale powdered activated carbon–membrane bioreactor (PAC–MBR) used for drinking water treatment were systematically examined by scanning electron microscopy (SEM), three-dimensional excitation emission matrix (EEM) fluorescence spectroscopy, Fourier transform infrared spectroscopy (FTIR) and energy diffusive X-ray (EDX) analysis. The results showed that external fouling, which comprised 31.68% of the total fouling, was caused by the deposition of a large amount of biological PAC on the membrane surface. Bacteria and organic matter comprised only a small fraction of the external foulants. Biologically derived proteins and polysaccharides were the major constituents of the internal foulants. EDX analysis indicated that the external and internal foulants also included inorganic elements such as Mg, Al, Si, Ca, Mn and Fe. During the operation of PAC–MBR, low flux and effective physical cleaning protocols should be adopted; proteins, polysaccharides and inorganic elements in the bioreactor should also be controlled.     

Review on modelling and control of desalination system using reverse osmosis

Dissolved salts in seawater or brackish water are reduced to a potable level through separation techniques, like, distillation, multiple effect vapor compression, evaporation, or by membrane processes such as electro-dialysis reversal, nano-filtration, and reverse osmosis (RO). RO is the most widely used desalination process. Recent advances in RO technology has led to more efficient separation and now is the most cost effective process to operate. The performance of the reverse osmosis process is dependent on concentration of dissolved solids in the feed-water, feed-water pressure, and the membrane strength to withstand system pressure, membrane solute rejection, membrane fouling characteristics, and the required permeate solute concentration. RO is a promising tool that uses cellulose acetate (or) polyamide membrane and is widely chosen as the cost of production is reduced by the use of energy efficient and process control techniques. This paper presents a review on modelling, identification of parameters from single input-outputs and multi input/output lumped systems, dynamic modelling and control of desalination systems in the past twenty years by collecting more than 60 literatures.     

Non-destructive approaches for assessing biofouling of household reverse osmosis membranes

Abstract

This study determined economic non-destructive methods to assess biofouling in point of use reverse osmosis (RO) membrane treatment systems. Three parallel household RO membrane units were operated under controlled feed water conditions to promote biofouling, inorganic fouling and a combination of both. Operational and biological parameters were monitored throughout the systems’ lifespan. Membrane autopsies assessed the degree and type of fouling. Statistical models determined statistically relevant parameters for fouling types that were validated with membrane autopsies. Permeate flow rates decreased differently with biofouling vs inorganic fouling. Large increases in permeate conductivity were noted in membranes suffering from biofouling and not in inorganically fouled membranes. The concentration of cell clumps from detached biofilm in the retentate increased in membranes experiencing biofouling and no increase was seen for inorganically fouled membranes. A combination of these methods could be used to conveniently assess the types of fouling experienced by RO systems.     

Reverse osmosis processing of organic model compounds and fermentation broths

Post-treatment of an anaerobic fermentation broth was evaluated using a 150 gal/day, single cartridge prototype reverse osmosis (RO) system. Baseline tests were conducted at 25 degrees C using six organic model compounds representing key species found in the fermentation broth: ethanol, butanol, acetic acid, oxalic acid, lactic acid, and butyric acid. Correlations of the rejection and recovery efficiencies for these organic species, individually and in simulated mixtures, were obtained as a function of feed pressure with and without recirculation of the retentate. The actual fermentation broth obtained from a continuous-flow biohydrogen process was treated by the RO system under the operating conditions similar to those used in the baseline tests, resulting in greater than 95% removal of total organic carbon. These results are encouraging and useful for further studies on the feasibility of incorporating the RO technology into an integrated and field deployable wastewater management and water recovery system.     

Membrane technology for surface water treatment: advancement from microfiltration to membrane bioreactor

Following the rapid proliferation of organic pollutants in the surface water, the application of microfiltration technology has been extensively studied for its treatment since the 1990s. Given that the conventional treatment processes were unable to treat the excessive dissolved organic compounds, microfiltration technologies have gained momentum as effective solutions to treat the surface water. The efficacy of low-pressure membrane filtration technologies such as microfiltration and ultrafiltration has been under scrutiny ever since, and numerous research studies have aimed at enhancing their capabilities to reject the suspended solids and organic matters. This paper reviews the development trajectory of membrane technology, ranging from microfiltration to membrane bioreactors, for treating dissolved organic matters in surface water and their future potential. This is a critical review of the physicochemical and biological options such as, but not limited to, pretreatment of water using coagulation, ozonation, adsorption and/or a combination of these. On the whole, it is concluded that the membrane bioreactor system, which combines biological process and physical rejection, showed high potential in treating polluted surface water, which needs to be further investigated extensively to promote its application in water treatment plants.     

Temporal and spatial patterns in salinity and suspended solids in a reservoir influenced by the Asian monsoon

Between April 1993 and November 1994, conductivity, cations, anions and suspended solids were measured at multiple sites in Taechung Reservoir, Korea. The major mechanism regulating ionic composition was dilution by monsoon rain and a resulting interflow current; these forces caused marked spatial and temporal heterogeneity. Ionic dilution was most pronounced in the headwaters during an intense monsoon in 1993 and was accompanied by an increase in the proportion of Na⁺and Cl^–, presumably from rainwater. A decrease of >25% in conductivity and cations occurred during summer 1993 at the plunge-point due to a temperature difference between the lake water and an interflow. In contrast, the 1994 monsoon was weak, ionic dilution was not apparent, and spatial-temporal variation was modest. Overall reservoir salinity was a direct function of water residence time which is regulated by monsoon intensity. Differences in hydrology between years also influenced seston composition; inorganic suspended solids dominated total suspended solids in 1993, but in 1994 the organic fraction was the major component.     

Magnetic supports for immobilized enzymes and bioaffinity adsorbents

Magnetic separation of immobilized enzymes or bioaffinity adsorbents allows their selective recovery from liquors containing other suspended solids, and gives easier handling of large numbers of samples in analysis. Non-porous magnetic supports seem to be more resistant to fouling, diffusional limitation and attrition than conventional porous supports. A variety of magnetic powders and linkage methods have been used in the preparation of supports, though it is not clear how many of these have the required properties for potential applications (including linkage stability, particle size and magnetic properties). Non-porous magnetic supports are attractive for use in liquors containing fouling materials or suspended solids, either for bioaffinity adsorbents or for immobilized enzymes acting on small molecular substrates. Magnetic supports also offer considerable advantages in analysis based on bioaffinity interactions, such as immunoassay.     

The freshwater tidal wetland Liberty Island,CA was both a source and sink of inorganic and organic material to the San Francisco Estuary

It is hypothesized that perennial freshwater tidal wetland habitat exports inorganic and organic material needed to support the estuarine food web and to create favorable habitat for aquatic organisms in San Francisco Estuary. It is also hypothesized that most of the material flux in this river-dominated region is controlled by river flow. The production and export of material by Liberty Island were measured and compared using discrete monthly and continuous (15 min) measurements of a suite of inorganic and organic materials and flow between 2004 and 2005. Seasonal material flux was estimated from monthly discrete data for inorganic nutrients, suspended solids and salts, organic carbon and nitrogen and phytoplankton and zooplankton group carbon and chlorophyll a and pheophytin pigment. Estimates of material flux from monthly values were compared with measured daily material flux values for chlorophyll a concentration, salt and suspended solids obtained from continuous measurements (15 min) using YSI water quality sondes. Phytoplankton carbon produced within the wetland was estimated by in situ primary productivity. Most inorganic and organic materials were exported from the wetland on an annual basis, but the magnitude and direction varied seasonally. Dissolved inorganic nutrients such as nitrate, soluble phosphorus, total phosphorus and silica as well as total suspended solids were exported in the summer while total and dissolved organic carbon were exported in the winter. Salts like chloride and bromide were exported in the fall. Chlorophyll a and pheophytin were exported in the fall and associated with diatom and cyanobacteria carbon. Mesozooplankton carbon was dominated by calanoid copepods and exported most of the year except summer. Continuous sampling revealed high hourly and daily variation in chlorophyll a, salt and total suspended solids flux due to high frequency changes in concentration and tidal flow. In fact, tidal flow rather than river discharge was responsible for 90% or more of the material flux of the wetland. These studies indicate that freshwater tidal wetlands can be a source of inorganic and organic material but the export of material is highly variable spatially and temporally, varies most closely with tidal flow and requires high frequency measurements of both tidal flow and material concentration for accurate estimates.     

Fertiliser drawn forward osmosis desalination: the concept, performance and limitations for fertigation

With the world??s population growing rapidly, pressure is increasing on the limited fresh water resources. Membrane technology could play a vital role in solving the water scarcity issues through alternative sources such as saline water sources and wastewater reclamation. The current generation of membrane technologies, particularly reverse osmosis (RO), has significantly improved in performance. However, RO desalination is still energy intensive and any effort to improve energy efficiency increases total cost of the product water. Since energy, environment and climate change issues are all inter-related, desalination for large-scale irrigation requires new novel technologies that address the energy issues. Forward osmosis (FO) is an emerging membrane technology. However, FO desalination for potable water is still a challenge because, recovery and regeneration of draw solutes require additional processes and energy. This article focuses on the application of FO desalination for non-potable irrigation where maximum water is required. In this concept of fertiliser drawn FO (FDFO) desalination, fertilisers are used as draw solutions (DS). The diluted draw solution after desalination can be directly applied for fertigation without the need for recovery and regeneration of DS. FDFO desalination can make irrigation water available at comparatively lower energy than the current desalination technologies. As a low energy technology, FDFO can be easily powered by renewable energy sources and therefore suitable for inland and remote applications. This article outlines the concept of FDFO desalination and critically evaluates the scope and limitations of this technology for fertigation, including suggestions on options to overcome some of these limitations.     

Microbial fouling of reverse-osmosis membranes used in advanced wastewater treatment technology: chemical, bacteriological, and ultrastructural analyses.

Biofouling of reverse-osmosis membranes was investigated at an advanced wastewater treatment facility. Cellulose diacetate membranes operated for approximately 4,000 h became uniformly coated with a mucilaginous fouling layer. The fouling material was approximately 93% water by weight, and nearly 90% of the dehydrated residue was organic in composition. Calcium, phosphorous, sulfur, and chlorine were the major inorganic constituents detected. Protein and carbohydrate represented as much as 30 and 17%, respectively, of the dry weight of the biofilm. Bacteriological plate counts indicated up to 5.6 X 10(6) CFU/cm2 of membrane surface. Accumulation of [3H]glucose in the biofilm and measurement of ATP indicated that the fouling bacteria were metabolically active in situ. The genus Acinetobacter and the Flavobacterium-Moraxella group were the major generic groups associated with the feedwater surface of the membrane, whereas species of the generic groups Acinetobacter, Pseudomonas-Alcaligenes, and Bacillus-Lactobacillus predominated on the permeate water surface. Electron microscopy revealed that the biofilm on the feedwater surface of the membrane was 10 to 20 microns thick and was composed of several layers of compacted bacterial cells, many of which were partially or completely autolyzed. The bacteria were firmly attached to the membrane surface by an extensive network of extracellular polymeric fibrils. Polyester (Texlon) support fibers located on the permeate surface of the reverse osmosis membranes were sparsely colonized, suggesting bacterial regrowth in the product water collection system.     

太湖梅梁湾水体中悬浮质及光谱的分布特征

在研究太湖梅梁湾水体中的悬浮质及水体中光谱分布时发现:总悬浮质中无机悬浮质含量与总悬浮质之间呈现明显的正比线形关系(R²=0.9724),而有机悬浮质与总悬浮质之间的正比线形关系较弱(R²=0.2921);在20cm处以下,总悬浮质中的藻类含量随着水深度的增加呈现下降的趋势,表面略低;有机悬浮质与叶绿素a的含量之间的线形关系较弱(R²=0.1344);光谱的分布特征是:在水体的表面,绿光最强,蓝光较强,而红光最弱;在150cm以下,红光最强,绿光较强,蓝光最弱。     

Effect of the pre-treatments for milk samples filtration on direct viable cell counts

Escherichia coli O25: H–42 was selected to study the effect of pre-treatments on the enumeration of direct viable cells from milk samples. Before and after inducing cell elongation by cellular division inhibitors, three pre-treatments for milk-filtration were used. One involved a pretreatment with trypsin (1·5 min at 50°C), addition of hot Triton X-100 after heating and filter rinses with phosphate saline buffer. The other two involved pretreatment with trypsin and Triton X-100 (10 min at 50°C), filter rinses with hot Triton X-100 and organic solvents. Pre-treatments applied after inducing cell elongation had an effect on cell recovery from milk samples depending on the pre-treatment used. The most suitable, on the basis of the number and percentage of enlarged cells obtained was the first described. The others selectively affected recovery of elongated cells. Pretreatments applied before inducing the cell elongation, negatively affected viability with enumerations in milk samples being significantly ( P < 0·001) lower than those found in controls. However, the negative effects of first pre-treatment on viability was lower than that produced by the pre-treatments involving organic solvents.     

Characterization and effect of biofouling on polyamide reverse osmosis and nanofiltration membrane surfaces

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.     

Optimising diquat use for submerged aquatic weed management

An experimentally derived prediction tool is under development which aims to assess potential deactivation of diquat caused by water and deposits on plant leaf surfaces in New Zealand water bodies, where aquatic weeds are targeted for diquat treatment. Optimising the use and success of diquat is important not only in managing public confidence in the use of aquatic herbicides, but also in minimising financial risk from failed treatments. Our approach focuses on characterising lake water quality and plant condition factors in these lakes to identify parameters that might be useful indicators of diquat deactivation potential. Water samples have been collected at 3-month intervals from lakes receiving large scale treatment for weed control. Samples have been analysed for turbidity, suspended solids, chlorophyll a, conductivity and dissolved anions. Samples have also been spiked with 1 mg l⁻¹ diquat to measure loss from adsorption and/or absorption. Shoot samples were also collected from targeted weed species at each sampling site and the amount of organic and inorganic deposits on plants has been measured and then added to a second diquat spiked sample to assess potential additional diquat loss from these deposits. Our results have shown deactivation from deposits on plant surfaces which is highly correlated with turbidity, including inorganic suspended solids and total suspended solids. A plant “dirtiness” scale has been devised to help predict the likely success or risk of diquat failure prior to any decision to proceed with treatment. Deactivation in water was only weakly linked to total suspended solids. Our failure to find significant correlation with the water quality factors measured may reflect the need for more detailed analysis of the particle size and composition of suspended solids and future research will address these issues.     

Pre-treatments to enhance the biodegradability of waste activated sludge: Elucidating the rate limiting step

Pre-treatments for waste activated sludge (WAS) are, in most cases, an attempt to increase the biodegradation and/or improve hydrolysis rate of WAS after anaerobic digestion. This review presents an extensive analysis of WAS pre-treatments effectiveness focusing on increasing the biodegradability. In the first part of the review, WAS is considered as a cluster of organic components: proteins, carbohydrates, humic substances and cells. Based on this breakdown into components, the effect of different pre-treatments on each component (and in combination) is described. Also, possible reasons for the contradictory results frequently found among different studies dealing with the same pre-treatment are included. In the second part, the review describes the effects on volatile solids removal by digestion after pre-treatment and on the dewaterability of the final digestate. The energy balance and potential limiting factors for each pre-treatment are also taken into account. From the published works it is concluded that some pre-treatment techniques, such as thermal hydrolysis, thermal phased anaerobic digestion and low-temperature pre-treatment are effective ways to increase energy production and to improve other sludge properties, such as dewatering. However, these techniques are very energy intensive and require a large capital outlay, so research on milder pre-treatment techniques is valuable.     

藻源污染物特性对高藻水微滤处理过程中膜污染的影响

采用不同生长时期的藻细胞、藻源型有机物(AOM)及原藻液进行过滤实验,研究不同生长时期的藻源污染物对膜污染的影响特性及机制。利用UMFI法分析不同生长时期的藻细胞、AOM及原藻液的污染程度;采用CRITIC分析法定量分析了不同生长时期的AOM和藻细胞在混合过滤过程中对膜污染的贡献率,同时采用混合污染堵塞模型分析了不同生长时期的原藻液不同过滤阶段的主要污染堵塞类型。结果表明, 3个生长时期的藻细胞及AOM的膜污染程度均为对数期最轻;值得注意的是,在原藻液过滤过程中藻细胞及AOM的膜污染贡献率随着生长时期的不同而有所变化,其中AOM的污染权重随着生长时期的延长不断减小,而藻细胞的污染权重随着生长时期的延长不断增大。不同生长时期的原藻液过滤过程中均呈现两段式污染堵塞类型,并且后段均为滤饼堵塞。研究不仅阐明了藻源型污染物特性对微滤处理高藻水膜污染的影响机制,同时也为改善膜污染的技术开发提供参考。     

Peracetic acid oxidation as an alternative pre-treatment for the anaerobic digestion of waste activated sludge

Anaerobic digestion is generally considered to be an economic and environmentally friendly technology for treating waste activated sludge, but has some limitations, such as the time it takes for the sludge to be digested and also the ineffectiveness of degrading the solids. Various pre-treatment technologies have been suggested to overcome these limitations and to improve the biogas production rate by enhancing the hydrolysis of organic matter. This paper studies the use of peracetic acid for disintegrating sludge as a pre-treatment of anaerobic digestion. It has been proved that this treatment effectively leads to a solubilisation of organic material. A maximum increase in biogas production by 21% is achieved. High dosages of PAA lead to a decrease in biogas production. This is due to the inhibition of the anaerobic micro-organisms by the high VFA-concentrations. The evolution of the various VFAs during digestion is studied and the observed trends support this hypothesis.     

A fluorescence-based indicator for nanofiltration fouling propensity caused by effluent organic matter (EfOM)

Effluent organic matter (EfOM) is one of the major foulants responsible for the occurrence of membrane fouling during advanced wastewater treatment using nanofiltration (NF) technology. In this present study, we have reported a simple fouling indicator based on the properties of fractional fluorescence and molecular weight, termed as fluorescence-size-index (FSI), to predict the fouling propensity of NF when filtrating EfOM. Specifically, EfOM collected from twenty-one real sewage samples were first analyzed to quantify their fluorescent compositions and concentrations. The results showed that the EfOM consisted mainly of humic-like substances, soluble organism metabolites and fulvic-like substances, characterized by small-molecule organic matters (<5 kDa) and hydrophobic fractions. Second, the major NF fouling fractions of EfOM were determined based on their fluorescent properties. It was observed that small-molecule hydrophobic components with humic-like fluorescence properties continuously influenced the flux decline rate throughout the whole operation, while macromolecular hydrophilic components with fluorescent properties of apparent aromatic hydrocarbon proteins were primarily responsible for the initial, rapid flux decline. Furthermore, the constructed FSI has proven to be useful in guiding the selection of pretreatment methods for preventing NF fouling.     

The status of membrane bioreactor technology

In this article, the current status of membrane bioreactor (MBR) technology for wastewater treatment is reviewed. Fundamental facets of the MBR process and membrane and process configurations are outlined and the advantages and disadvantages over conventional suspended growth-based biotreatment are briefly identified. Key process design and operating parameters are defined and their significance explained. The inter-relationships between these parameters are identified and their implications discussed, with particular reference to impacts on membrane surface fouling and channel clogging. In addition, current understanding of membrane surface fouling and identification of candidate foulants is appraised. Although much interest in this technology exists and its penetration of the market will probably increase significantly, there remains a lack of understanding of key process constraints such as membrane channel clogging, and of the science of membrane cleaning.     

Anaerobic degradation pathway and kinetics of domestic wastewater at low temperatures

The effect of temperatures below 20 °C (20, 15 and 10 °C) on the anaerobic degradation pathway and kinetics of domestic wastewater fractionated at different sizes was studied in a fluidized-bed batch reactor. The overall degradation pathway was characterized by a soluble fraction degrading according to zero-order kinetics and a colloidal fraction (between 0.45 and 4.5 μm) that first disintegrates into a particulate fraction smaller than 0.45 μm before finally degrading. The colloidal degradation processes follow a first-order kinetic. In contrast, suspended solids (bigger than 4.5 μm) degrade to soluble and colloidal fractions according to first-order kinetics. The colloidal fraction originating from suspended solids further degrades into soluble fraction. These soluble fractions have the same degradation kinetics as the original soluble fraction. The suspended solids degradation was highly affected by temperature, whereas the soluble fraction slightly affected and the colloidal fraction was not affected at all. On the other hand, the colloidal non-degradable fraction increased significantly with the decrease in temperature while the suspended solids slowly increased. The soluble non-degradable fraction was little affected by temperatures changes.