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What Is Environmental Microbiology?
The study of how microorganisms affect the earth and its atmosphere is called environmental microbiology or microbial ecology. Environmental microbiology is the study of microbes in the environment and their interactions with each other. Microbes are the tiniest creatures on Earth, yet despite their small size, they have a have a huge impact on us and on our environment. Most types of microbes remain unknown. It is estimated that we know fewer than 1% of the microbial species on Earth. Yet microbes surround us everywhere -- air, water, soil. An average gram of soil contains one billion (1,000,000,000) microbes representing probably several thousand species. Environmental microbiology is the study of the relationships that exist between microorganisms and the environment. Environmental microbiology is the relationship of microorganisms with themselves and with their surroundings. Microorganisms have special impact on the whole biosphere. They are the backbone of ecosystems of the zones where light cannot approach. In such zones, chemosynthetic bacteria are present which provide energy and carbon to the other organisms there. Some microbes are decomposers which have ability to recycle the nutrients. So, microbes have a special role in biogeochemical cycles. Microbes, especially bacteria, are of great importance in the sense that their symbiotic relationship (either positive or negative) have special effects on the ecosystem. Bacteria and their enzymes, along with some fungi and critical nutrient additives are cost effective agents for in-situ remediation of hazardous wastes and subsurface pollution in soils, sediments and wastewaters. The ability of each bacteria strain to degrade toxic waste depends on the nature of each contaminant. Since most sites are typically comprised of multiple pollutant types, the most effective approach to bioremediation is to use a mixture of bacterial species/strains, each specific to the degradation of one or more types of contaminants. It is critical to monitor the composition of the indigenous and added bacterial consortium in order to evaluate the activity level of the bacteria, and to permit modifications of the nutrients and other conditions for optimizing the bioremediation process. Environmental Microbiology - overview: The pervasive and manifold positive and negative impacts of microbial activities on human and environmental health, and human activities, require that efforts to improve the human condition include efforts to modulate microbial activities. Attainment of this goal will be greatly facilitated by acquisition of a fundamental understanding of microbial functioning in their natural settings, and of parameters that regulate such activities. Our current fragmentary knowledge of microbial processes is based largely on information obtained from individual strains of microbes studied in the laboratory as pure, exponentially-growing cultures in nutrient-rich, homogeneous aqueous solutions. Sewage treatment is the process that removes the majority of the contaminants from waste-water or sewage and produces both a liquid effluent suitable for disposal to the natural environment and a sludge. To be effective, sewage must be conveyed to a treatment plant by appropriate pipes and infrastructure and the process itself must be subject to regulation and controls. Sewage is the liquid waste from toilets, baths, showers, kitchens, etc. that is disposed of via sewers. In many areas sewage also includes some liquid waste from industry and commerce. In the UK, the waste from toilets is termed foul waste, the waste from items such as basins, baths, kitchens is termed sullage water, and the industrial and commercial waste is termed trade waste. The division of household water drains into Greywater and Black water is becoming more common in the United States, with greywater being permitted to be used for watering plants or recycled for flushing toilets. Much sewage also includes some surface water from roofs or hard-standing areas. Municipal wastewater therefore includes residential, commercial, and industrial liquid waste discharges, and may include stormwater runoff. Sewerage systems that transport liquid waste discharges and stormwater together to a common treatment facility are called combined sewer systems. The construction of combined sewers is a less common practice in the U.S. and Canada than in the past and is no longer accepted within Building Regulations in the UK. Instead, liquid waste and stormwater are collected and conveyed in separate sewer systems, referred to as sanitary sewers and storm sewers in the U.S. and as foul sewers and surface water sewers in the UK. Overflows from foul sewers designed to relieve pressure from heavy rainfall are termed storm sewers or combined sewer overflows. As rainfall runs over the surface of roofs and the ground, it may pick up various contaminants including soil particles (sediment), metals, organic compounds, animal waste, and oil and grease. Some jurisdictions, such as certain communities located in southern California, require stormwater to receive some level of treatment before being discharged to the environment. Examples of treatment processes used for stormwater include sedimentation basins, wetlands, and vortex separators (to remove coarse solids). "Conventional wastewater treatment" is the process used in modern wastewater treatment plants that removes the majority of the contaminants from wastewater. This produces a liquid effluent suitable for disposal to the natural environment and also produces a sludge. The treatment process typically involves the following three stages: Primary treatment Primary treatment is to reduce oils, grease, fats, sand, grit, and coarse (settleable) solids. Grit removal This stage typically includes a grit channel where the velocity of the incoming wastewater is carefully controlled to allow grit and stones to settle but still maintain all organic material within the flow. Grit and stones need to be removed early in the process to avoid damage to pumps and equipment in the remaining treatment stages. Screening or maceration The grit free liquid is then passed through fixed or rotating screens to remove larger material such as rags. Screenings are collected and may be returned to the sludge treatment plant or may be disposed of off site by landfilling or incineration. Maceration, in which solids are cut into small particles through the use of rotating knife edges mounted on a revolving cylinder, is used in plants that are able to process this particulate waste. Macerators are, however, more expensive to maintain and are less reliable than physical screens. Sedimentation Primary sedimentation tank at a rural treatment plantIn almost all plants there is a sedimentation stage where the sewage is allowed to stand in large tanks so that faecal solids can settle and floating material such as grease and plastics can rise to the surface and be skimmed off. The main purpose of the primary stage is to produce a generally homogeneous liquid capable of being treated biologically together with a sludge that can be separately treated or processed. Primary settlement tanks are usually equipped with mechanically driven scrapers that continually drive the collected sludge towards a hopper in the base of the tank from where it can be pumped to further sludge treatment stages. Secondary treatment Secondary treatment is designed to substantially degrade the biological content of the sewage. The majority of municipal and industrial plants treat the settled sewage liquor using aerobic biological processes. For this to be effective, the biota require both oxygen and a substrate on which to live. There are number of ways in which this is done. In all these methods, the bacteria and protozoa consume biodegradable soluble organic contaminants (e.g. sugars, fats, organic short-chain carbon molecules, etc.) and bind much of the less soluble fractions into floc particles. Roughing Filters Roughing filters are intended to treat particularly strong or variable organic loads. They are typically tall, columnar filters filled with open synthetic filter media to which sewage is applied at a relatively high rate. The design of the filters allows high hydraulic loading and a high flow-through of air. The resultant liquor is usually within the normal range for conventional treatment processes. Activated sludge Activated sludge plants use a variety of mechanisms and processes to use dissolved oxygen to generate a biological floc that substantially removes organic material. It also traps particulate material and can, under ideal conditions, convert ammonia to nitrite or nitrate. Filter Beds Trickling filter bed using plastic mediaIn older plants and plants receiving more variable loads, trickling filter beds are used where the settled sewage liquor is spread onto the surface of a deep bed made up of coke (carbonised coal), rocks or specially fabricated plastic media with high surface areas. The liquor is distributed through perforated rotating arms radiating from a central pivot. The distributed liquor trickles through this bed and is collected in drains at the base. These drains also provide a source of air which percolates up through the bed, keeping it aerobic. Biological film comprising of bacteria, protozoa and fungi forms on all the available surfaces and this provides the required biological treatment capability to effect the reduction in organic content. Rotating Plates and Spirals In some smaller plants slowly revolving plates or spirals are used which are partially submerged in the liquor. A biotic floc is created which provides the required substrate. Secondary sedimentation The final step in the secondary treatment stage is to settle out the biological floc or filter material and produce an effluent with very low levels of organic material and suspended matter. Secondary Sedimentation tank at a rural treatment plantTertiary treatment Tertiary treatment provides a final stage to raise the effluent quality to the standard required before it is discharged to the receiving environment (sea, river, lake, ground, etc.) More than one tertiary treatment process may be used at any treament plant. If disinfection is practiced, it is always the final process. Effluent polishing Sand filtration Sand filtration removes much of the residual suspended matter. Lagooning Lagoons provides settlement and further biological improvement through storage in large man-made ponds or lagoons. Constructed wetlands These include engineered reed beds and a range of similar methodologies, all of which provide a high degree of aerobic biological improvement and can often be used instead of secondary treatment for small communities. Nutrient removal Wastewater may also contain high levels of nutrients (nitrogen and phosphorus) that in certain forms may be toxic to fish and invertebrates at very low concentrations(e.g. ammonia) or that can create nuisance conditions in the receiving environment (e.g. weed or algal growth). Although the growth of weeds and algae may seem to be primarily an aesthetic issue, algae can produce toxins, and in dying their decay and consumption by bacteria in the environment can result in the depletion of oxygen in the water and the possible consequential suffocation of fish. Where receiving rivers discharge to lakes or shallow seas, the added nutrients can cause severe and sometimes irreversible eutrophication with the loss of many sensitive clean water species. The removal of nitrogen and/or phosphorus from wastewater can be achieved either biologically or by chemical precipitation treatment processes. Nitrogen removal Biological treatment of nitrogen generally involves creating conditions within the treatment process for bacteria to convert the ammonia to nitrate, and then allowing other bacteria to reducing the nitrate to nitrogen gas, which is released to the atmosphere. Sand filters, lagooning and the use of reed beds can all be used to reduce nitrogen. Sometimes the conversion of toxic ammonia to nitrate alone is referred to as tertiary treatment. Phosphorous removal The biological treatment of wastewater to remove phosphorus also involves the design and creation of specific environmental conditions within a treatment plant to enable specific bacteria to bio-accumulate large quantities of phosphorus. When the bacteria containing the phosphorus are removed, the resulting bacterial biosolids often have a high fertilizer value. Phosphorus can also be removed by chemical precipitation using (commonly) salts of iron (i.e. ferric chloride) or aluminum (i.e. alum). The resulting chemical sludge, however, is difficult to dispose of, and the use of chemicals in the treatment process is expensive and makes operation difficult and often messy. Disinfection Disinfecting substantially reduces the numbers of living organisms in the water to be discharged. The effectiveness of disinfection depends on the quality of the water being treated, the type of disinfection being used, the application rate, the contact time and environmental variables. Turbid water will be treated less successfully since solid matter can shield organisms, especially from Ultraviolet light or if contact times are low. Generally, short contact times, low doses and high flows all mitigate against effective disinfection. Common methods of disinfection include ozone, chlorine, or UV light. Chloramine, which is used for drinking water, is not used in waste water treatment because of its persistence. Int J Syst Evol Microbiol, 2005 Jan, 55(Pt 1), 433 - 436Nocardia takedensis sp . nov., isolated from moat sediment and scumming activated sludge; Yamamura H et al.; Chemotaxonomic and morphological characterization of two actinomycete strains, MS1-3(T) and AS4-2, respectively isolated from moat sediment and scumming activated sludge, was carried out . This characterization clearly demonstrated that strains MS1-3(T) and AS4-2 belong to the genus Nocardia . 16S rRNA gene sequencing studies showed that these isolates are most closely related to Nocardia beijingensis (98.1-98.3 % similarity), Nocardia brasiliensis (97.9-98.0 %) and Nocardia tenerifensis (97.8-97.9 %) . However, the results of DNA-DNA hybridizations and physiological and biochemical tests showed that strains MS1-3(T) and AS4-2 could be differentiated from their closest phylogenetic relatives both genotypically and phenotypically . It is proposed that the two isolates be classified as representatives of a novel species of Nocardia, Nocardia takedensis sp . nov . The type strain is MS1-3(T) (=NBRC 100417(T)=DSM 44801(T)); AS4-2 (=NBRC 100418=DSM 44802) is a reference strain. Int J Syst Evol Microbiol, 2005 Jan, 55(Pt 1), 363 - 368 Shewanella decolorationis sp . nov., a dye-decolorizing bacterium isolated from activated sludge of a waste-water treatment plant; Xu M et al.; A highly efficient dye-decolorizing bacterium, strain S12(T), was isolated from activated sludge of a textile-printing waste-water treatment plant in Guangzhou, China . The cells were Gram-negative and motile by means of a single polar flagellum . The strain was capable of anaerobic growth either by fermentation of glucose or by anaerobic respiration and utilized a variety of electron acceptors, including nitrate, iron oxide and thiosulfate . The physiological properties, tested by using the Biolog GN2 system, were similar to those of the genus of Shewanella . Analysis of the nearly complete 16S rRNA gene sequence of strain S12(T) showed the highest similarity (98 and 97 %, respectively) to Shewanella baltica and Shewanella putrefaciens . However, the level of gyrB similarity between strain S12(T) and S . putrefaciens was 87 % . DNA from strain S12(T) showed 41.8 and 41.9 % DNA relatedness, respectively, to the DNA of S . baltica DSM 9439(T) and S . putrefaciens DSM 6067(T) . The DNA G+C content of strain S12(T) was 49.3 mol% . The predominant menaquinone was MK-7 and the predominant ubiquinones were Q-7 and Q-8 . The dominant fatty acids were 15 : 0, 16 : 0, iso-15 : 0 and 16 : 1omega7c, similar to the profiles of other Shewanella species . On the basis of its physiological and molecular properties, strain S12(T) appears to represent a novel species of the genus Shewanella, for which the name Shewanella decolorationis sp . nov . is proposed . The type strain is S12(T) (=CCTCC M 203093(T)=IAM 15094(T)). Int J Syst Evol Microbiol, 2005 Jan, 55(Pt 1), 341 - 344 Hydrogenophaga defluvii sp . nov . and Hydrogenophaga atypica sp . nov., isolated from activated sludge; Kampfer P et al.; Two Gram-negative, oxidase-positive rods (strains BSB 9.5(T) and BSB 41.8(T)) isolated from wastewater were studied using a polyphasic approach . 16S rRNA gene sequence comparisons demonstrated that both strains cluster phylogenetically within the family Comamonadaceae: the two strains shared 99.9 % 16S rRNA gene sequence similarity and were most closely related to the type strains of Hydrogenophaga palleronii (98.5 %) and Hydrogenophaga taeniospiralis (98.0 %) . The fatty acid patterns and substrate-utilization profiles displayed similarity to the those of the five Hydrogenophaga species with validly published names, although clear differentiating characteristics were also observed . The two strains showed DNA-DNA hybridization values of 51 % with respect to each other . No close similarities to any other Hydrogenophaga species were detected in hybridization experiments with the genomic DNAs . On the basis of these results, two novel Hydrogenophaga species, Hydrogenophaga defluvii sp . nov . and Hydrogenophaga atypica sp . nov . are proposed, with BSB 9.5(T) (=DSM 15341(T)=CIP 108119(T)) and BSB 41.8(T) (=DSM 15342(T)=CIP 108118(T)) as the respective type strains. FEMS Microbiol Rev, 2005 Jan, 29(1), 49 - 64 "Microthrix parvicella", a filamentous bacterium causing bulking and foaming in activated sludge systems: a review of current knowledge; Rossetti S et al.; This review summarizes the microbiology and physiology of "Microthrix parvicella" and the methods of its growth control in activated sludge wastewater treatment plants . This filamentous bacterium is of high interest because of its worldwide involvement in severe bulking and foaming at wastewater treatment plants . We present a critical analysis of physiological and kinetic data on "M . parvicella" and discuss its growth and storage abilities in various environments with the aim of understanding the strategies of this organism to successfully compete with other bacteria in activated sludge . Additionally, this review elaborates on research needs for defining reliable control strategies of bulking and foaming based on key features of "M . parvicella". Environ Toxicol Chem, 2004 Dec, 23(12), 2790 - 8 Effect of ethoxylate number and alkyl chain length on the pathway and kinetics of linear alcohol ethoxylate biodegradation in activated sludge; Itrich NR et al.; Batch activated-sludge die-away studies were conducted with various pure homologs to determine the effect of ethoxylate number and alkyl chain length on the kinetics of primary and ultimate biodegradation of linear alcohol ethoxylates . The 14C-(ethoxylate) homologs C14E1, C14E3, C14E6, and C14E9 were used to investigate the effect of ethoxylate number, and 14C-(ethoxylate) homologs C12E6, C14E6, and C16E6 were used to examine the effect of chain length . Activated sludge was dosed with a trace concentration (0.2 microM) of each homolog, and the disappearance of parent, formation of metabolites, production of 14CO2, and uptake into solids were monitored with time . Ethoxylate number had little effect on the first-order decay rates for primary biodegradation, which ranged from 61 to 78 h(-1) . However, alkyl chain length had a larger effect, with the C16 chain-length homolog exhibiting a slower rate of parent decay (18 h(-1)) compared to its corresponding C12 and C14 homologs (61-69 h(-1)) . Ethoxylate number affected the mechanism of biodegradation, with fission of the central ether bond to yield the corresponding fatty alcohol and (poly)ethylene glycol group increasing in dominance with increasing ethoxylate number . Based upon the measured rates of primary biodegradation, removal of parent during activated-sludge treatment was predicted to range between 99.7 and 99.8% for all homologs except C16E6, which had a predicted removal of 98.9% . Based upon the measured rates of ultimate biodegradation, removal of ethoxylate-containing metabolites was predicted to exceed 83% for all homologs . These predictions corresponded closely with previously published removal measurements in laboratory continuous activated-sludge systems and actual treatment plants. Appl Microbiol Biotechnol . 2005 Jan 13; {Epub ahead of print} Influence of substrate surface loading on the kinetic behaviour of aerobic granules; Liu Y et al.; In the aerobic granular sludge reactor, the substrate loading is related to the size of the aerobic granules cultivated . This study investigated the influence of substrate surface loading on the growth and substrate-utilization kinetics of aerobic granules . Results showed that microbial surface growth rate and surface biodegradation rate are fairly related to the substrate surface loading by the Monod-type equation . In this study, both the theoretical maximum growth yield and the Pirt maintenance coefficient were determined . It was found that the estimated theoretical maximum growth yield of aerobic granules was as low as 0.2 g biomass g(-1) chemical oxygen demand (COD) and 10-40% of input substrate-COD was consumed through the maintenance metabolism, while experimental results further showed that the unit oxygen uptake by aerobic granules was 0.68 g oxygen g(-1) COD, which was much higher than that reported in activated sludge processes . Based on the growth yield and unit oxygen uptake determined, an oxidative assimilation equation of acetate-fed aerobic granules was derived; and this was confirmed by respirometric tests . In aerobic granular culture, about 74% of the input substrate-carbon was converted to carbon dioxide . The growth yield of aerobic granules was three times lower than that of activated sludge . It is likely that high carbon dioxide production is the main cause of the low growth yield of aerobic granules, indicating a possible energy uncoupling in aerobic granular culture. Appl Microbiol Biotechnol . 2005 Jan 13; {Epub ahead of print} Comparing activated sludge and aerobic granules as microbial inocula for phenol biodegradation; Tay ST et al.; Activated sludge and acetate-fed granules were used as microbial inocula to start up two sequencing batch reactors (R1, R2) for phenol biodegradation . The reactors were operated in 4-h cycles at a phenol loading of 1.8 kg m(-3) day(-1) . The biomass in R1 failed to remove phenol and completely washed out after 4 days . R2 experienced initial difficulty in removing phenol, but the biomass acclimated quickly and effluent phenol concentrations declined to 0.3 mg l(-1) from day 3 . The acetate-fed granules were covered with bacterial rods, but filamentous bacteria with sheaths, presumably to shield against toxicity, quickly emerged as the dominant morphotype upon phenol exposure . Bacterial adaptation to phenol also took the form of modifications in enzyme activity and increased production of extracellular polymers . 16S rRNA gene fingerprints revealed a slight decrease in bacterial diversity from day 0 to day 3 in R1, prior to process failure . In R2, a clear shift in community structure was observed as the seed evolved into phenol-degrading granules without losing species-richness . The results highlight the effectiveness of granules over activated sludge as seed for reactors treating toxic wastewaters. J Environ Qual, 2005 Jan-Feb, 34(1), 105 - 13 Processes for managing pathogens; Godfree A et al.; Wastewater contains human, animal, and plant pathogens capable of causing viral, bacterial, or parasitic infections . There are several routes whereby sewage pathogens may affect human health, including direct contact, contamination of food crops, zoonoses, and vectors . The range and numbers of pathogens in municipal wastewater vary with the level of endemic disease in the community, discharges from commercial activities, and seasonal factors . Regulations to control pathogen risk in the United States and Europe arising from land application of biosolids are based on the concept of multiple barriers to the prevention of transmission . The barriers are (i) treatment to reduce pathogen content and vector attraction, (ii) restrictions on crops grown on land to which biosolids have been applied, and (iii) minimum intervals following application and grazing or harvesting . Wastewater treatment reduces number of pathogens in the wastewater by concentrating them with the solids in the sludge . Although some treatment processes are designed specifically to inactivate pathogens, many are not, and the actual mechanisms of microbial inactivation are not fully understood for all processes . Vector attraction is reduced by stabilization (reduction of readily biodegradable material) and/or incorporation immediately following application . Concerns about health risks have renewed interest in the effects of treatment (on pathogens) and advanced treatment methods, and work performed in the United States suggests that Class A pathogen reduction can be achieved less expensively than previously thought . Effective pathogen risk management requires control to the complete chain of sludge treatment, biosolids handling and application, and post-application activities . This may be achieved by adherence to quality management systems based on hazard analysis critical control point (HACCP) principles. Water Res, 2005 Jan-Feb, 39(2-3), 456 - 68 Epub 2004 Dec 08. Evaluation of microscopic techniques (epifluorescence microscopy, CLSM, TPE-LSM) as a basis for the quantitative image analysis of activated sludge; Lopez C et al.; Microscopic techniques ranging from epifluorescence microscopy to confocal laser scanning microscopy (CLSM) and two photon excitation laser scanning microscopy (TPE-LSM) combined with fluorescent stains can help to evaluate complex microbial aggregates such as activated sludge flocs . To determine the application limits of these microscopic techniques, activated sludge samples from three different sources were evaluated after staining with a fluorescent viability indicator (Baclight Bacterial Viability Kit, Molecular Probes) . Image analysis routines were developed to quantify overall amounts of red and green stained cells, location of stained cells within the flocs, and the spatial organization in clusters and filaments . It was found that the selection of the appropriate microscopic technique depends strongly on the type of microbial aggregates being analyzed . For flocs with high cell density, the use of TPE-LSM is preferred, since it provides a clearer image of the internal structure of the aggregate . Epifluorescence microscopy did not allow to reliably quantify red stained cells in dense aggregates . CLSM did not adequately image the internal filamentous structure and the location of stained cells within dense flocs . However, for typical activated sludge flocs epifluorescence and CLSM proved adequate. J Biotechnol, 2005 Feb 9, 115(3), 317 - 28 Parallel hybrid modeling methods for a full-scale cokes wastewater treatment plant; Lee DS et al.; Parallel hybrid modeling methods are applied to a full-scale cokes wastewater treatment plant . Within the hybrid model structure, a mechanistic model specifies the basic dynamics of the relevant process and a non-parametric model compensates for the inaccuracy of the mechanistic model . First, a simplified mechanistic model is developed based on Activated Sludge Model No . 1 and the specific process knowledge of the cokes wastewater treatment process . Then, the mechanistic model is combined with five different non-parametric models - feedforward back-propagation neural network, radial basis function network, linear partial least squares (PLS), quadratic PLS and neural network PLS (NNPLS) - in parallel configuration . These models are identified with the same data obtained from the plant operation to predict dynamic behavior of the process . The performance of each parallel hybrid model is compared based on their ease of model building, prediction accuracy and interpretability . For this application, the parallel hybrid model with NNPLS as non-parametric model gives better performance than other parallel hybrid models . In addition, the NNPLS model is used to analyze the behavior of the operation data in the reduced space and allows for fault detection and isolation. Microbiology, 2005 Jan, 151(Pt 1), 301 - 9 Recovery of an environmental chlamydia strain from activated sludge by co-cultivation with Acanthamoeba sp; Collingro A et al.; Chlamydiae are a unique group of obligate intracellular bacteria comprising important pathogens of vertebrates as well as symbionts of free-living amoebae . Although there is ample molecular evidence for a huge diversity and wide distribution of chlamydiae in nature, environmental chlamydiae are currently represented by only few isolates . This paper reports the recovery of a novel environmental chlamydia strain from activated sludge by co-cultivation with Acanthamoeba sp . The recovered environmental chlamydia strain UV-7 showed the characteristic morphology of chlamydial developmental stages as revealed by electron microscopy and was identified as a new member of the family Parachlamydiaceae (98.7 % 16S rRNA sequence similarity to Parachlamydia acanthamoebae) . Infection studies suggested that Parachlamydia sp . UV-7 is not confined to amoeba hosts but is also able to invade mammalian cells . These findings outline a new straightforward approach to retrieving environmental chlamydiae from nature without prior, tedious isolation and cultivation of their natural host cells, and lend further support to suggested implications of environmental chlamydiae for public health. J Hazard Mater, 2005 Jan 31, 117(2-3), 161 - 70 Fenton peroxidation improves the drying performance of waste activated sludge; Dewil R et al.; Advanced sludge treatment processes (AST) reduce the amount of sludge produced and improve the dewaterability, thus probably also affecting the heat transfer properties and the drying characteristics of the sludge . This paper studies the influence of the Fenton peroxidation on the thermal conductivity of the sludge . Results demonstrate that the Fenton's peroxidation positively influences the sludge cake consistency and hence enhances the mechanical dewaterability and the drying characteristics of the dewatered sludge . For the two sludges used in this study, i.e . obtained from the wastewater treatment plants (WWTP) of Tienen and Sint-Niklaas - the dry solids content of the mechanically dewatered sludge increased from 22.5% to 40.3% and from 18.7% to 35.2%, respectively . The effective thermal conductivity k(e) of the untreated and the peroxidized sludges is measured and used to determine the heat transfer coefficient h(s) . An average improvement for k(e) of 16.7% (Tienen) and 5.8% (Sint-Niklaas) was observed . Consequently the value of h(s) increased with 15.6% (Tienen) and 5.0% (Sint-Niklaas) . This increased heat transfer coefficient in combination with the increased dewaterability has direct implications on the design of sludge dryers . A plate-to-plate calculation of a multiple hearth dryer illustrates that the number of plates required to dry the peroxidized sludge to 90% DS is less than half the number of plates needed to dry untreated sludge . This results in reduced dryer dimensions or a higher capacity for an existing dryer of given dimensions. FEMS Microbiol Lett, 2005 Jan 15, 242(2), 367 - 73 Discrepancies in the widely applied GAM42a fluorescence in situ hybridisation probe for Gammaproteobacteria; Siyambalapitiya N et al.; A bacterial culture collection of 104 strains was obtained from an activated sludge wastewater treatment plant to pursue studies into microbial flocculation . Characterisation of the culture collection using a polyphasic approach indicated seven isolates, phylogenetically affiliated with the deep-branching Xanthomonas group of the class Gammaproteobacteria, were unable to hybridise the GAM42a fluorescence in situ hybridisation (FISH) probe for Gammaproteobacteria . The sequence of the GAM42a probe target region in the 23S rRNA gene of these isolates was determined to have mismatches to GAM42a . Probes perfectly targeting the mismatches (GAM42a_T1038_G1031, and GAM42a_T1038 and GAM42a_A1041_A1040) were synthesised, and used in conjunction with GAM42a in FISH to study the Gammaproteobacteria community structure in one full-scale activated sludge plant . Several bacteria in the activated sludge biomass bound the modified probes demonstrating their presence and the fact that these Gammaproteobacteria have been overlooked in community structure analyses of activated sludge. Chemosphere, 2005 Feb, 58(5), 605 - 14 Effect of copper in the protistan community of activated sludge; Nicolau A et al.; Protists have proved to be an interesting tool for assessing the occurrence of pollution in wastewater treatment systems along with its role in the control of pollution itself through grazing of dispersed bacteria and maintenance of a healthy trophic web in those artificial ecosystems . Two sets of assays were carried on in a bench scale pilot plant in order to study the response of the activated sludge community of protists to the exposure of copper: the first set was carried on with synthetic sewage and the second one with real sewage . The results emphasize the ability of activated sludge biological communities to survive and to react to toxicants and highlight the role of protistan communities as indicators of toxicants entrance in treatment systems. Chemosphere, 2005 Feb, 58(5), 543 - 50 Toxicity of metals and organic chemicals evaluated with bioluminescence assays; Ren S et al.; The development of a bioluminescent sensor organism (Shk1) that was created for assessing wastewater toxicity was reported several years ago . In order to establish a test battery to better characterize wastewater toxicity, additional luminescent sensor organisms were later created . The present study focused on one promising candidate (PM6), a Pseudomonas spp . strain, because of its high level of luminescence compared to that of other newly created organisms . Using a batch toxicity testing protocol, the toxicity of 7 metals and 25 organic compounds was evaluated with the PM6 and Shk1 assays . Results indicated that the toxicity data of the PM6 and the Shk1 assays were correlated, and no assay appeared to be particularly more sensitive to a group of toxicants than the other assay . The results of the PM6 and Shk1 assays were further evaluated by comparing with the results of the Vibrio fischeri luminescence inhibition assay and activated sludge inhibition assays . Data suggested that PM6 and Shk1 more closely represented activated sludge organisms than V . fischeri . The suitability of using PM6 and Shk1 for assessing wastewater toxicity on activated sludge, both individually and in a test battery, was discussed. Environ Pollut, 2005 Apr, 134(3), 431 - 8 Aerobic biodegradation of organotin compounds in activated sludge batch reactors; Stasinakis AS et al.; The biodegradation behavior of four organotin (OT) compounds, namely tributyltin (TBT), dibutyltin (DBT), monobutyltin (MBT) and triphenyltin (TPhT), was studied in lab-scale activated sludge batch reactors . The activated sludge was spiked with the OT compounds at a level of 100mugl(-1) as Sn . Determination of the OT compounds by GC-FPD after ethylation in the dissolved and particulate phase revealed that 24h after the start of the experiments, almost the total of OT compounds has been removed from the dissolved phase and is associated with the suspended solids . Calculation of mass balance in batch reactors showed that OT compounds biodegradation was performed via a sequential dealkylation process . Removals due to biodegradation were differentiated according to the parent compound . In experiments with non-acclimatized biomass, a percentage of 27.1, 8.3, 73.8 and 51.3 was still present as TBT, DBT, MBT and TPhT, respectively, at the end of the experiment (18th day) . Half-lives (t(1/2)) of 10.2 and 5.1 days were calculated for TBT and DBT, respectively, whereas apparent t(1/2) values could not be determined for MBT and TPhT (t(1/2)>18 days) . The capacity of activated sludge to biodegrade OT compounds in the absence of supplemental substrate indicated that these compounds can be metabolized as single sources of carbon and energy in activated sludge systems . Excluding TBT, the presence of low concentrations of supplemental substrate did not affect the biodegradation potential of activated sludge . The acclimatization of biomass on OT compounds enhanced significantly biodegradation, resulting in significant decreases of half-lives of OT compounds . As a result in the presence of acclimatized biomass, half-lives of 1.4, 3.6, 9.8 and 5.0 days were calculated for TBT, DBT, MBT and TPhT, respectively. Biosci Biotechnol Biochem, 2004 Dec, 68(12), 2457 - 65 Genes Involved in Aniline Degradation by Delftia acidovorans Strain 7N and Its Distribution in the Natural Environment; Urata M et al.; Aniline-degraders were isolated from activated sludge and environmental samples and classified into eight phylogenetic groups . Seven groups were classified into Gram-negative bacteria, such as Acidovorax sp., Acinetobacter sp., Delftia sp., Comamonas sp., and Pseudomonas sp., suggesting the possible dominance of Gram-negative aniline-degraders in the environment . Aniline degradative genes were cloned from D . acidovorans strain 7N, and the nucleotide sequence of the 8,039-bp fragment containing eight open reading frames was determined . Their deduced amino acid sequences showed homologies to glutamine synthetase (GS)-like protein, glutamine amidotransferase (GA)-like protein, large and small subunits of aniline dioxygenase, reductase, LysR-type regulator, small ferredoxin-like protein, and catechol 2,3-dioxygenase, suggesting a high similarity of this gene cluster to those in P . putida strain UCC22 and Acinetobacter sp . strain YAA . Polymerase chain reaction (PCR) and sequencing analyses of GS-like protein gene segments of other Gram-negative bacteria suggested that Gram-negative bacteria have aniline degradative gene that can be divided into two distinctive groups. Syst Appl Microbiol, 2004 Nov, 27(6), 646 - 52 Leucobacter chromiireducens sp . nov, and Leucobacter aridicollis sp . nov., two new species isolated from a chromium contaminated environment; Morais PV et al.; Two strains designated strains L-1T and L-9T were isolated from activated sludge of a treatment plant that receives wastewater from the tannery industry contaminated with chromium . Phylogenetic analysis showed that the organisms represented two new species of the genus Leucobacter . Strains L-1T and L-9T could be distinguished from the type strain of L . komagatae and from the type strain of "L . albus" by the B-type peptidoglycan composition, fatty acid composition, several phenotypic and physiological characteristics . The major fatty acids of the organisms were iso- and anteiso-branched C15:0 and C17:0, straight-chain C16:0 was also found in relatively high proportions . The organisms were halotolerant, grew in medium containing 9% NaCl, and all strains, including the type strain of L . komagatae grew in medium containing 5 mM Cr(VI) . On the basis of the distinct peptidoglycan composition, 16S ribosomal DNA sequence analysis, percentage of DNA-DNA reassociation values, and phenotypic characteristics we are of the opinion that strain L-1T represents a new species of the genus Leucobacter for which we propose the name Leucobacter chromiireducens and that strain L-9T represents an additional new species of the same genus for which we propose the name Leucobacter aridicollis. Water Res, 2005 Jan, 39(1), 97 - 106 The solids retention time-a suitable design parameter to evaluate the capacity of wastewater treatment plants to remove micropollutants; Clara M et al.; Micropollutants as endocrine disrupting compounds (EDC) or pharmaceuticals are of increased interest in water pollution control . Wastewater treatment plant (WWTP) effluents are relevant point sources for residues of these compounds in the aquatic environment . The solids retention time (SRT) is one important parameter for the design of WWTPs, relating to growth rate of microorganisms and to effluent concentrations . If a specific substance is degraded in dependency on the SRT, a critical value for the sludge age can be determined . In WWTPs operating SRTs below this critical value, effluent concentrations in the range of influent concentrations or a distribution according to the adsorption equilibrium have to be expected, whereas in WWTPs operating at SRTs higher than the critical value degradation will occur . Critical SRTs were determined for different micropollutants, indicating that the design criteria based on the sludge age allows an estimation of emissions . Different treatment technologies as conventional activated sludge systems and a membrane bioreactor were considered and no significant differences in the treatment efficiency were detected when operated at comparable SRT . The results of the investigations lead to the conclusion that low effluent concentrations can be achieved in WWTPs operating SRTs higher than 10 days (referred to a temperature of 10 degrees C) . This corresponds to the requirements for WWTPs situated in sensitive areas according to the urban wastewater directive of the European Community (91/271/EEC) in moderate climatic zones. Water Res, 2005 Jan, 39(1), 59 - 64 Reduction of bromate to bromide coupled to acetate oxidation by anaerobic mixed microbial cultures; van Ginkel CG et al.; Bromate, a weakly mutagenic oxidizing agent, exists in surface waters . The biodegradation of bromate was investigated by assessing the ability of mixed cultures of micro-organisms for utilization of bromate as electron acceptor and acetate as electron donor . Reduction of bromate was only observed at relatively low concentrations (<3.0mM) in the absence of molecular oxygen . Under these conditions bromate was reduced stoichiometrically to bromide . Unadapted sludge from an activated sludge treatment plant and a digester reduced bromate without lag period at a constant rate . Using an enrichment culture adapted to bromate, it was demonstrated that bromate was a terminal electron acceptor for anaerobic growth . Approximately 50%of the acetate was utilized for growth with bromate by the enrichment culture . A doubling of 20h was estimated from a logarithmic growth curve . Other electron acceptors, like perchlorate, chlorate and nitrate, were not reduced or at negligible rates by bromate-utilizing microorganisms. Environ Sci Pollut Res Int, 2004, 11(6), 379 - 87 Fate of Ah receptor agonists during biological treatment of an industrial sludge containing explosives and pharmaceutical residues; Gustavsson LK et al.; GOAL, SCOPE AND BACKGROUND: Sweden is meeting prohibition for deposition of organic waste from 2005 . Since 1 million tons of sludge is produced every year in Sweden and the capacity for incineration does not fill the demands, other methods of sludge management have to be introduced to a higher degree . Two biological treatment alternatives are anaerobic digestion and composting . Different oxygen concentrations result in different microbial degradation pathways and, consequently, in a different quality of the digestion or composting residue, It is therefore necessary to study sludge treatment during different oxygen regimes in order to follow both degradation of compounds and change in toxicity . In this study, an industrial sludge containing explosives and pharmaceutical residues was treated with anaerobic digestion or composting, and the change in toxicity was studied . Nitroaromatic compounds, which are the main ingredients of both pharmaceutical and explosives, are well known to cause cytotoxicity and genotoxicity . However, little data are available concerning sludge with nitroaromatics and any associated dioxin-like activity . Therefore, we studied the sludge before and after the treatments in order to detect any changes in levels of Ah receptor (AhR) agonists using two bioassays for dioxin-like compounds . METHODS: An industrial sludge was treated with anaerobic digestion or composting in small reactors in a semi-continuous manner . The same volume as the feeding volume was taken out daily and stored at -20 degrees C . Sample preparation for the bioassays was done by extraction using organic solvents, followed by clean up with silica gel or sulphuric acid, yielding two fractions . The fractions were dissolved in DMSO and tested in the bioassays . The dioxin-like activity was measured using the DR-CALUX assay with transfected H4IIE rat hepatoma pGudluc cells and an EROD induction assay with RTL-W1 rainbow trout liver cells . RESULTS AND DISCUSSION: The bioassays showed that the sludge contained AhR agonists at levels of TCDD equivalents (TEQs) higher than other sludge types in Sweden . In addition, the TEQ values for the acid resistant fractions increased considerably after anaerobic digestion, resulting in an apparent formation of acid resistant TEQs in the anaerobic reactors . Similar results have been reported from studies of fermented household waste . There was a large difference in effects between the two bioassays, with higher TEQ levels in the RTL-W1 EROD assay than in the DR-CALUX assay . This is possibly due to a more rapid metabolism in rat hepatocytes than in trout hepatocytes or to differences in sensitivities for the AhR agonists in the sludge . It was also demonstrated by GC/FID analysis that the sludge contained high concentrations of nitroaromatics . It is suggested that nitroaromatic metabolites, such as aromatic amines and nitroanilines, are possible candidates for the observed bioassay effects . It was also found that the AhR agonists in the sludge samples were volatile . CONCLUSIONS: The sludge contained fairly high concentrations of volatile AhR agonists . The increase of acid resistant AhR agonist after anaerobic digestion warrants further investigations of the chemical and toxic properties of these compounds and of the mechanisms behind this observation . RECOMMENDATION AND OUTLOOK: This study has pointed out the benefits of using different types of mechanism-specific bioassays when evaluating the change in toxicity by sludge treatment, in which measurement of dioxin-like activity can be a valuable tool . In order to study the recalcitrant properties of the compounds in the sludge using the DR-CALUX assay, the exposure time can be varied between 6 and 24 hours . The properties of the acid-resistant AhR agonists formed in the anaerobic treatment have to be investigated in order to choose the most appropriate method for sludge management. Appl Microbiol Biotechnol . 2004 Dec 16; {Epub ahead of print} Reduction of excess sludge production by 3,3',4', 5-tetrachlorosalicylanilide in an activated sludge process; Ye FX et al.; The potential of 3,3',4',5-tetrachlorosalicylanilide (TCS) addition to an activated sludge continuous process to reduce excess sludge production by disrupting coupling between anabolism and catabolism was investigated . TCS was chosen as a metabolic uncoupler for continuous test in a lab-scale completely mixed activated sludge process . TCS reduced sludge yield by approximately 30% at a dosage of 40 mg/day . Substrate removal capability was not adversely affected by the presence of TCS, but effluent nitrogen concentration increased during the 60-day continuous operation . Sludge settleability of treated and control samples was qualitatively comparable and not significantly different . Microbial activities in terms of specific oxygen uptake rate were also enhanced, and the microbial population was altered . The results suggest that TCS is an effective chemical uncoupler that reduces sludge yield; process performance was not significantly affected by introduction of the uncoupler. J Microbiol Methods, 2005 Feb, 60(2), 195 - 205 Stability of the fluorogenic enzyme substrates and pH optima of enzyme activities in different Finnish soils; Niemi RM et al.; Fluorogenic artificial substrates facilitate sensitive enzyme activity measurements for a variety of processes in soil and other environmental samples . It is possible to use in situ pH for measurements on condition that the substrates are chemically stable . We studied the stability of 12 different methyl umbellipherone (MUF) and amino methyl coumarine (AMC) derivatives used as substrates for arylsulphatase, alpha-glucosidase, beta-glucosidase, beta-xylosidase, cellobiosidase, chitinase, phosphomonoesterase (PME), phoshodiesterase (PDE), esterase, lipase and alanine- and leucine aminopeptidases (AP) over the pH range from 4.0 to 8.0 in modified universal buffer (MUB) . Stability of the substrates for lipase (4-MUF-heptanoate) and esterase (4-MUF-acetate) measurements was poor, especially at the higher pH values . Chitinase substrate, 4-MUF-N-acetyl-beta-d-glucosamide, was unstable at high pH values whereas the substrate for PME activity measurement (4-MUF-phosphate) disintegrated at low pH . The other substrates and MUF and AMC standard solutions were stable over the pH range studied . The optima between pH 4 and 8 of the 11 different enzyme activities were measured in three forest and two agricultural soil samples and in one activated sludge sample . In soil, for alanine and leucine AP the pH optima were usually 7.5 or higher, for arylsulphatase, beta-glucosidase, beta-xylosidase, esterase and PDE between 4 and 5.5, and for cellobiosidase between 4 and 5 . alpha-Glucosidase had an optimum below 5.5 but also exhibited high activity at pH 7 . Soil-dependent variation in pH optima were observed for chitinase, esterase, PDE and PME . Enzyme activities were also measured in 0.5 M acetate buffer at pH 5.5 . This buffer yielded the highest activities in all soil samples for arylsulphatase, PDE and PME. Environ Res, 2005 Mar, 97(3), 245 - 57 Persistent organic pollutants (POPs) in the conventional activated sludge treatment process: fate and mass balance; Katsoyiannis A et al.; The fate and the mass balance of persistent organic pollutants (POPs) during the conventional activated sludge treatment process were investigated in the wastewater treatment plant of the city of Thessaloniki, northern Greece . The POPs of interest were 7 polychlorinated biphenyls and 19 organochlorine pesticides . Target compounds were determined at six different points across the treatment system: the influent, the effluent of the primary sedimentation tank, the effluent of the secondary sedimentation tank, the primary sludge, the activated sludge from the recirculation stream, and the digested/dewatered sludge . The distribution of POPs between the dissolved and the adsorbed phases of wastewater and sludge was investigated . A good linear relationship between the distribution coefficients, K(d), and the octanol-water partition coefficients, K(ow), of the solutes was observed only in raw wastewater, suggesting that other factors affect the phase distribution of organic compounds in treated wastewater . For all POPs, a significant increase in partitioning with a decreasing solids concentration was observed, revealing an effect from non-settling microparticles remaining in the "dissolved" phase during the separation procedure . A good linear relationship was also revealed between logK(d) and the dissolved organic carbon (DOC) content of wastewater, suggesting that DOC favors the advective transport of POPs in the dissolved phase . Almost all POPs showed good mass balance agreements at both the primary and the secondary treatment . The losses observed for some species could be attributed to biodegradation/biotransformation rather than volatilization . The relative distribution between the treated effluent and the waste sludge streams varied largely among different compounds, with p-p'-DDE being highly accumulated in the waste sludge (98%) but almost 60% of alpha-HCH remaining in the treated effluent. Water Sci Technol, 2004, 50(9), 213 - 21 Recovery of energy from sludge--comparison of the various options; Rulkens WH et al.; This paper gives a general discussion of existing sludge treatment processes and of innovative treatment options, especially focused on the valuable use of organic carbon compounds as an energy source . Attention is paid both to high and to low temperature processes and to combinations of these processes . Based on an assessment and comparison the most beneficial and sustainable options are identified and a rough indication is given of the possibilities for improvement and future developments. Water Sci Technol, 2004, 50(9), 197 - 204 Sludge as source of energy and revenue; Onyeche TI; Sludge is a residue/product from wastewater treatment plants and contains most of the contaminants released during human activities . Some stringent environmental regulations on sludge treatment and disposal exist in many countries . This has resulted in increasing interest in sludge treatment methods that encourage sludge reduction and improvement in biogas production during anaerobic digestion processes . This work demonstrates the first exploitation of valuable energy from homogenised sludge at technical scale with mass reduction . The optimal combination of sludge homogenisation at relatively low pressures using a modified high-pressure homogeniser led to the success of this unique project . Results showed that about 30% more energy could be obtained from thickened and disrupted sludge than from untreated samples . The energy produced was higher than that invested during disruption and digestion processes . About 23% sludge reduction was also observed with no increase in chemical oxygen demand . This new process can produce extra energy for local electrification and heating the digester while the sludge reduction provides economic benefits . Concentration of sludge causes reduction in investment cost on digester as well as reduction in operational time for sludge dewatering. Water Sci Technol, 2004, 50(9), 161 - 8 Direct generation of electricity from sludges and other liquid wastes; Dentel SK et al.; Recently it has been shown that electrical energy can be harvested from marine sediments, simply by connection of an electrode (anode) in anaerobic marine sediments to an electrode in the aerobic zone above the sediments . We have now shown that similar applications are available in sludge treatment . Using a reactor with graphite foil electrodes in an aerated aerobic and anaerobic sludge zone, electrical current was generated, and enhanced when an additional organic substrate (acetate) was added . Electron microscopy, x-ray diffraction, and PCR examination of the anode surface showed no surface colonization and no increase in Geobacter relative to a control, indicating that microbial use of the anode as an electron acceptor wa indirect through the use of redox mediators . Given the demonstration of electricity generation from sludge, the potential for similar applications, using other organic waste sources, is evaluated. Water Sci Technol, 2004, 50(9), 129 - 36 Physical characteristics of a waste activated sludge: conditioning responses and correlations with a synthetic surrogate; Dursun D et al.; The efficient and economic management of waste activated sludge (WAS) requires a proper understanding of the sludge's material properties . Though there has been much study of WAS, an adequate linkage between its physical and chemical properties has been elusive . In particular, the conditioning and dewatering of WAS are expensive operations, and the addition of polymer to WAS leads to even more complex material behavior that is difficult to optimize . This paper reports on an extensive characterization of WAS, both with and without polymer conditioning . We combined the classical "jar test" approach with less conventional rheometric and electrokinetic measurements . In addition to the use of sampled WAS, a synthetic surrogate sludge was formulated, attempting to duplicate properties of WAS and allow more extensive characterization of a reproducible surrogate to WAS . Results with both the synthetic surrogate and WAS indicated that the traditional, electrokinetic, and rheological properties were related . However, the dose optima by rheometry were somewhat higher in both cases. Water Sci Technol, 2004, 50(9), 121 - 8 Minimization of sludge production and stable operational condition of a submerged membrane activated sludge process; Bhatta CP et al.; Modification of conventional activated sludge process by adding microfiltration type hollow fiber membrane module offers various advantages . The membrane module is immersed directly in the bioreactor to separate the treated water from the sludge and the modified process is called submerged membrane activated sludge process (SMASP) . Bench scale SMASP units were operated at constant flux to study the possibility of minimizing the excess sludge production and stable operation at different SRT and BOD loading . The long SRT developed high stabilized MLSS concentration in the bioreactor and decreased the sludge loading rate {kg-BOD/kg-MLSS-d} . In SMASP, very low sludge yield coefficients (0.04-0.09 kg-MLSS/kg-BOD) were obtained at long SRT (500 d) and small BOD loading (< or =0.5 kg/(m3 x d)) as compared to conventional activated sludge process and these coefficients showed considerable minimization in excess activated sludge production . At the same operation conditions, suction pressure was also maintained low (<25 kPa), and then SMASP was operated stably for long time (approximately 200 d). Water Sci Technol, 2004, 50(9), 41 - 8 Co-conditioning and dewatering of alum sludge and waste activated sludge; Lai JY et al.; Co-conditioning and dewatering behaviors of alum sludge and waste activated sludge were investigated . Two different sludges were mixed at various ratios (2:1; 1:1; 1:2; 1:4) for study . Capillary suction time (CST) and specific resistance to filtration (SRF) were utilized to assess sludge dewaterability . Relatively speaking, waste activated sludge, though of higher solid content, was more difficult to be dewatered than alum sludge . It was found that sludge dewaterability and settlability became better with increasing fraction of alum sludge in the mixed sludge . Dosage required of the cationic polyelectrolyte (KP-201C) for dewatering was reduced as well . It is proposed that alum sludge acts as skeleton builder in the mixed sludge, and renders the mixed sludge more incompressible which is beneficial for sludge dewatering. e, a, g. Implications of the results of the study to the sludge management plan for Taipei City that generates both alum sludge and waste activated sludge at significant amount are also discussed . The current sludge treatment and disposal plan in Metropolitan Taipei could be made more cost-effective. Water Sci Technol, 2004, 50(9), 25 - 32 Ultrasonic sludge treatment for enhanced anaerobic digestion; Hogan F et al.; Ultrasound is the term used to describe sound energy at frequencies above 20 kHz . High-powered ultrasound can be applied to a waste stream via purpose-designed tools in order to induce cavitation . This effect results in the rupture of cellular material and reduction of particle size in the waste stream, making the cells more amenable to downstream processing . sonix is a new technology utilising high-powered, concentrated ultrasound for conditioning sludges prior to further treatment . This paper presents recent results from a number of demonstration and full-scale plants treating thickened waste activated sludge (TWAS) prior to anaerobic digestion, therefore enhancing the process . The present studies have proved that the use of ultrasound to enhance anaerobic digestion can be achieved at full scale and effectively result in the TWAS (typically difficult to digest) behaving, after sonication, as if it were a "primary" sludge . The technology presents benefits in terms of increased biogas production, better solids reduction, improved dewatering characteristics of the digested sludge mixture and relatively short payback periods of two years or less subject to the site conditions and practices applicable at that time. Environ Sci Technol, 2004 Nov 1, 38(21), 5632 - 41 Three-dimensional dual-morphotype species modeling of activated sludge flocs; Martins AM et al.; An individual-based model, originally developed for a biofilm system, was adapted to simulate three-dimensional formation of activated sludge flocs . The model was extended to two different bacterial morphotypes (floc-forming and filamentous bacteria), allowing spatial development of the floc according to the bacterial morphology, diffusion, reaction, and growth processes . The model needed also extension with a process for attachment of individual cells . Despite being in an early stage of development, the model is already a tool that enables us to obtain useful information about the microfloc environment . The model indicates that filamentous bacterial morphology and substrate microgradients are important aspects in the formation of bacterial structures . In mass transport-limited regimes filamentous bacterial structures prevail, whereas in growth-limited regimes irregular shaped flocs with fingerlike structures are dominant . These modeling results suggest that activated sludge flocs and biofilms might be different manifestations of the same phenomena . The model results support the hypothesis that floc-macrogradients can be the most important parameter for development of bulking sludge . The model suggests that attachment has a very strong effect on floc structure, leading to enhancement of the effect of substrate microgradients. J Colloid Interface Sci, 2005 Jan 1, 281(1), 136 - 45 Physicochemical properties and stability of activated sludge flocs under temperature upshifts from 30 to 45 degrees C; Morgan-Sagastume F et al.; The impacts of temperature shifts from 30 to 45 degrees C on the structural stability and surface charge of activated sludge flocs were assessed in four sequencing batch reactors (SBRs) treating pulp and paper mill effluent . The improvement in floc stability was tested by sludge magnesium enrichment in one SBR and by operating another reactor at a high sludge retention time (SRT) of 33 days . Floc stability was characterized by dissociation constants with solutions of CaCl(2), KCl, urea, and ethylenediamine tetraacetate (EDTA) . Surface charge was assessed by cationic-anionic titration and metals concentrations were also determined . The temperature shift consistently caused an increase in the negative sludge surface charge from approximately -0.180 to -0.300 meq/g MLSS . Magnesium enrichment and a high SRT of 33 days promoted less negatively charged sludge, dampened the increase in negative sludge surface charge, and yielded structurally stronger flocs; however, sludge deflocculation still occurred . Manganese and iron appeared to be released by sludge under the temperature shift . It was concluded that the temperature shift deteriorates the flocculating physicochemical properties of the sludge and that better floc stability achieved by magnesium enrichment and a high SRT is not enough to stop deflocculation . Further research is required to clarify the origin of the increase in negative sludge surface charge, the role of metals, and the governing factors in sludge deflocculation under such temperature shifts. J Microbiol Methods, 2005 Jan, 60(1), 1 - 11 Optimized sequence retrieval from single bands of temperature gradient gel electrophoresis profiles of the amplified 16S rDNA fragments from an activated sludge system; Zhang X et al.; Sequence retrieval from single bands of polymerase chain reaction (PCR)-denaturing gel electrophoresis (DGE) profiles is an important but often difficult step for molecular diversity analysis of complex microbial communities such as activated sludge systems . We analyzed the temperature gradient gel electrophoresis (TGGE) profiles of PCR-amplified 16S rDNA fragments from an activated sludge sample of a coking wastewater treatment plant . Single bands were excised, and a clone library was constructed for each . Sequence heterogeneity in each single band was found to be significantly overestimated due to single-stranded DNA (ssDNA) contamination formed during the PCR amplification, since only 10-60% of library clones of each single TGGE band had identical migration behavior compared with the parent band . Three methods, digestion with mung bean nuclease, optimization of PCR amplification, and purification via denatured polyacrylamide gel electrophoresis (d-PAGE), were compared for their ability to minimize ssDNA contamination, with the last one being the most efficient . After using d-PAGE to minimize ssDNA to a nearly nondetectable level, 70-100% of library clones for each single TGGE band had identical migration compared with the parent band . Several sequences were found in each of six single bands, and this co-migration could be predicted with the Poland software . The predominant bacteria of the activated sludge were assessed via a combination of sequence retrieval from each single TGGE band and band intensity analysis . Only beta and alpha subclasses of the Proteobacteria were detected, 93.8% and 6.2%, respectively . Our work suggests that prior to constructing a clone library to retrieve the actual sequence diversity of a single DGE band, it is advisable to minimize ssDNA contamination to a nondetectable level. Water Sci Technol, 2004, 50(8), 193 - 200 High rate treatment by aerobic upflow sludge blanket (AUSB) with external oxygenation; Sharma KR et al.; A 3-year study was conducted using an aerobic upflow sludge blanket (AUSB) reactor to achieve high-rate biological treatment through maintenance of a high biomass concentration (7-10 g VSS/L) together with a high oxygen flux . The AUSB reactor was not aerated directly; instead, oxygenation was provided in an external chamber with flow recirculation . The oxygenation was provided at four different pressurizations: 0, 15, 20 and 25 psig . The AUSB reactor was also pressurized to avoid the flotation of biomass . The flow recirculation rate was varied from 400% to 1,500% in order to ensure adequate oxygen supply . It was found that the AUSB system was able to handle a volumetric loading of as high as 10 kg COD/m3-day with a removal efficiency of 92% . Despite a high upflow velocity through AUSB, the effluent suspended solid concentration was mostly below 60 mg/L . The active fraction of biomass in the AUSB sludge was about 3 times higher than that of the regular activated sludge . This was indicated by a very high specific oxygen uptake rate (SOUR), up to 180-250 mg O2/g VSS-hr . The sludge yield in the entire system was only 0.09 to 0.13 g VSS/g COD removed . This was mainly caused by additional auto-oxidation of biosolids in the oxygenation chamber due to flow recirculation. Water Sci Technol, 2004, 50(8), 177 - 83 Effect of chlorination bulking control on water quality and phosphate release/uptake in an anaerobic-oxic activated sludge system; Chang WC et al.; This study evaluates the effect of chlorination bulking control on water quality and phosphate release/uptake in an anaerobic-oxic activated sludge system . A series of batch experiments with different specific NaOCl mass dose were conducted to determine the sludge settling properties, supernatant water quality and phosphate metabolism behavior of filamentous bulking sludge . The harvested sludge was from a continuous-flow anaerobic-oxic (A/O) activated sludge pilot-plant, i.e., enhanced biological phosphorus removal (EBPR) system, operated with 15 days of sludge retention time . The filamentous bacteria in the A/O pilot plant were identified to be Thiothrix according to Eikelboom's classification techniques, which was in accordance with the high influent sulfate concentration of this study (50 mg/L sulfate) . Increasing NaOCI concentration, as revealed by experimental results, obviously decreased the sludge settling properties (SVI values and zone settling velocities) and meanwhile significantly reduced supernatant water quality (COD, SS, TP) mainly due to higher suspended solids caused by floc disruption . Moreover, the nine-hour batch experiments indicated that high NaOCI dosage (40 mg/gMLSS) completely deteriorated phosphate metabolism of EBPR sludge . Such a high dosage of chlorination further confirmed overdosing through disappearance of intracellular PHB and death of protozoa by microscopic investigation . Still, phosphate release/uptake behavior of EBPR sludge properly functions at low NaOCl dosage (5 mg/g MLSS) . Besides, phosphate metabolism worsens rapidly before the SVI value reaches its lowest level . These findings imply that determining NaOCI requirement with merely SVI values can readily result in chlorination overdosing . Proper NaOCI dosage requires a delicately balanced consideration between sludge settling improvement, water quality demand and phosphate metabolism . Batch test of phosphate release/uptake is apparently a prerequisite to conclude an appropriate NaOCl dosage for bulking control. Water Sci Technol, 2004, 50(8), 153 - 9 Microbial degradation of estrogens using activated sludge and night soil-composting microorganisms; Shi JH et al.; In order to investigate the potential for microbial degradation of estrogens, and the products formed, activated sludge collected from Korea (ASK) and night soil-composting microorganisms (NSCM) were used to degrade estrogens . Results showed that both ASK and NSCM degraded almost 100% of the natural estrogens estrone (E1), 17beta-estradiol (E2), and estriol (E3) from initial concentrations of 20-25 mg/L, while synthetic estrogen, ethynylestradiol (EE2), was not degraded . Analysis of degradation products of E2 by using HPLC-ECD and a consecutive first-order reaction calculation confirmed that E2 was sequentially degraded to E1, which was further degraded to other unknown compounds by ASK and NSCM . We then used the yeast two-hybrid assay to show that the unknown degradation products did not appear to possess estrogenic activity when E1, E2 or E3 were degraded to below the detection limit after 14 days of incubation, indicating that ASK and NSCM not only degrade natural estrogens, but also remove their estrogenic activities. Water Sci Technol, 2004, 50(8), 135 - 43 Effects of phosphorus limitation and temperature on PHA production in activated sludge; Chinwetkitvanich S et al.; The study was designed to investigate the effects of temperature and phosphorus limitation on polyhydroxyalkanoate (PHA) production and storage by activated sludge biomass . The two-stage operation approach, i.e . a growth phase followed by a nutrient limitation phase, was applied to induce PHA accumulation . The pre-selected temperatures of 10, 20 and 30 degrees C were investigated under phosphorus limitation conditions using three four-litre fully aerobic SBR systems operated at an SRT of 10 days with cycle time and HRT of 6 and 10 hours . PHA production was greater in the 10 degrees C system than in the 20 degrees C and 30 degrees C systems but there was little difference between the two higher temperatures . The maximum PHA fractions of the sludge were 52, 45 and 47%TSS for the three temperatures from low to high, and the maximum PHA concentrations in the mixed liquors were 1,491, 1,294 and 1,260 mg/l, respectively . However, it was observed that very low values of PHA yield per unit COD consumed were obtained, i.e., 0.05, 0.03 and 0.04 mgPHA/mgCODu, for the 10, 20 and 30 degrees C reactors, respectively . This was because all three systems required several days to reach maximum PHA accumulation in their mixed liquor biomasses . It is probable the bacteria still had some stored poly-P in their cells upon initiation of the phosphorus limited influent, and PHA accumulation was delayed until the stored phosphorus was depleted . Also, PHA productivity was reduced by the large amounts of biomass lost from the systems because of sludge bulking. Water Sci Technol, 2004, 50(8), 125 - 33 Sludge thickening performance of mesh filtration process; Park MS et al.; Small-scale wastewater treatment facilities play an important role in improving the aquatic environment in many countries . Although sludge treatment is essential for overall wastewater treatment, it is difficult for small-scale facilities to use mechanical equipment or other facilities . As the first step of the sludge treatment, it is important to develop a convenient sludge thickening process for small-scale facilities . In this work, we examined the sludge thickening performance of a mesh filtration system: the mesh opening sizes of 100-500 microm, and the sludge (3,000-9,000 mg-SS/L) was obtained from a domestic wastewater treatment facility . The filtration was carried out only under the hydraulic pressure between the water level and the effluent port connected to the mesh filter module . The sludge reduction rates were in the range of 85-95% for 6-7 h; the initial filtration rate was very high, but the rate decreased with a decrease in hydraulic pressure due to the reduction of the water level in the vessel . In addition, the effluents (passed through the mesh) contained very low SS and could be directly discharged into the environment. J Hazard Mater, 2004 Dec 10, 116(1-2), 159 - 66 Biological treatability of raw and ozonated penicillin formulation effluent; Cokgor EU et al.; In the present study, oxidative pre-treatment of pharmaceutical wastewater originating from the formulation of the penicillin Sultamycillin Tosylate Diydrate via ozonation at varying pH and ozone feed rates was investigated . Biological treatability studies were performed with a synthetic wastewater alone and supplemented with raw and ozonated penicillin formulation effluents . The highest COD (34%) and TOC (24%) removal efficiencies were obtained at pH 11.0, whereas the BOD5 value increased from 16 mg l(-1) to 128 mg l(-1) after 40 min of ozonation, corresponding to an applied ozone dose of 1670 mg l(-1) and 33% relative ozone absorption . The studies showed that no degradation of raw penicillin fraction (30% of total COD) occurred, and degradation of the synthetic wastewater being completely treatable without penicillin addition, was inhibited by 7% . Upon 40 min ozonation, the synthetic wastewater could be completely oxidized and at the same time 35% of ozonated penicillin wastewater removal was obtained . Respirometric studies were conducted in parallel and produced results indicating a 22% decrease in the total oxygen consumption rate established for raw penicillin formulation effluent compared to the results obtained from the aerobic batch reactor . No inhibition of the synthetic fraction was observed for the 40 min-ozonated penicillin formulation effluent, biodegradability of the 60 min-ozonated penicillin effluent decreased possibly due to recalcitrant oxidation product accumulation . The modeling study provided experimental support and information on inhibition kinetics in activated sludge model no . 3 (ASM3) by means of respirometric tests for the first time. Water Sci Technol, 2004, 50(7), 287 - 92 Reduction of coagulant amount added to activated sludge for phosphorus removal; Nakajima J et al.; Adding coagulant to the activated sludge process is effective in maintaining the stability of phosphorus removal . However, the precise mechanisms of the reaction and behavior of coagulants and phosphorus are not well known . By introducing a new phosphorus removal model (PRM), the behavior of coagulant and phosphorus in the process could be described . The experimental data of the effluent phosphorus concentration and Fe content in the activated sludge agreed with the values calculated by PRM . The amount of coagulant addition to the activated sludge process for phosphorus removal is reduced with the enhanced biological phosphorus removal process . It is suggested that the amount of reduction is determined by using PRM. Water Sci Technol, 2004, 50(7), 281 - 5 Monitoring activated sludge settling properties using image analysis; Jenne R et al.; The goal of this study is to develop a monitoring system for activated sludge properties, as this is an essential tool in the battle against filamentous bulking . A fully automatic image analysis procedure for recognising and characterising flocs and filaments in activated sludge images has been optimised and subsequently used to monitor activated sludge properties in a lab-scale installation . The results of two experiments indicate that the image information correlates well with the Sludge Volume Index . It is shown that, at the onset of filamentous bulking, there is an increase in total filament length on the one hand, and a change in floc shape on the other hand. Water Sci Technol, 2004, 50(7), 249 - 55 Performances of three R-AN-D-N wastewater treatment plants in the Czech Republic; Bejvl Z et al.; The evolution of Czech standards requires higher efficiency of nutrient removal from municipal wastewaters . At the beginning of the last decade of 20th century, a new activated sludge configuration called R-AN-D-N process has been described, successfully tested and now largely used at several wastewater treatment plants (WWTP) in the Czech republic . The main feature of the R-AN-D-N process is the introduction of a regeneration zone in sludge recycle, which enables to increase sludge age in the system without any substantial increase in WWTP volume . Performances of three Czech large WWTP with R-AN-D-N configuration have been monitored and compared within a period of one and a half years . The results confirmed excellent nutrient removal efficiency for wastewaters with different proportion between sewage and industrial effluents . Two of three monitored WWTP received wastewaters from breweries (Budweiser and Pilsner Urquell) . The settleability of activated sludge from all three WWTP was correct, with SVI values usually ranging from 50 to 150 ml/g . Monitoring of sludge composition indicated proliferation of several filamentous bacteria, particularly types 0581, 0092 and M . parvicella . No severe bulking events were observed . Finally, the operational costs expressed in CZK (Czech crown: 1 CZK = {see symbol in text}0.0322) per cubic metre of treated sewage or per capita amounts respectively from 2.24 to 6.52, and from 285 to 342. Water Sci Technol, 2004, 50(7), 221 - 8 North American performance experience with anoxic and anaerobic selectors for activated sludge bulking control; Parker D et al.; Obtaining reliably high compaction characteristics and low SVI values has enormous economic consequences on activated sludge plant design and operation . Now that use of selectors has become more common for achieving low SVI values, the assessment of the full-scale performance characteristics of activated sludge plants incorporating selectors has high value for the design and operation of future plants . Treatment plant effluent quality is seldom analyzed solely on an average basis and the impact peak events have on effluent quality must be considered in design and operation . Descriptive statistics should also be used to assess selector performance, so that the influence of infrequently occurring values on plant design and operation can be assessed . The performance of 21 activated sludge plants incorporating selectors was evaluated . All the selector plants for which post installation data were available showed that the operating SVI values were significantly improved . One plant studied in detail showed that final effluent quality was significantly better after the selector installation . As a group, activated sludge plants with anaerobic selectors outperform those with anoxic selectors . Dissolved oxygen control is just as important in activated sludge plants with selectors as in conventional activated sludge plants. Water Sci Technol, 2004, 50(7), 179 - 86 Influence of sludge properties and hydraulic loading on the performance of secondary settling tanks--full-scale operational results; Vestner RJ et al.; Full-scale investigations at a WWTP with a two-stage secondary settling tank process revealed relationships between significant operating parameters and performance in terms of effluent suspended solids concentration . Besides common parameters (e.g . surface overflow rate and sludge volume loading rate) feed SS concentration and flocculation time must be considered . Concentration of the return activated sludge may help to estimate the performance of existing secondary settling tanks. Water Sci Technol, 2004, 50(7), 123 - 30 Modeling of a large-scale wastewater treatment plant for efficient operation; Gokcay CF et al.; Environmental legislations in the Western world impose stringent effluent quality standards for ultimate protection of the environment . This is also observed in Turkey . The current paper presents efforts made to simulate an existing 0.77 million m3/day conventional activated sludge plant located at Ankara, AWTP . The ASM1 model was used for simulation in this study . The model contains numerous stoichiometric and kinetic parameters, some of which need to be determined on case by case bases . The easily degradable COD (S(S)) was determined by two methods, physical-chemical and respirometric methods, namely . The latter method was deemed unreliable and rejected in the further study . Dynamic simulation with SSSP program predicted effluent COD and MLSS values successfully while overestimating OUR . A complete fit could only be obtained by introducing a dimensionless correction factor (etaO2 = 0.58) to the oxygen term in ASM1. Water Sci Technol, 2004, 50(7), 61 - 8 A control strategy for reducing aeration costs during low loading periods; Sahlmann C et al.; The efficiency of the aeration system in a full-scale activated sludge basin with 3 separately controlled aeration zones was improved for the low loading period in summer . The air flow rate to each aeration zone is currently regulated to hold a preset dissolved oxygen concentration (DO) . Four different DO setpoint combinations were tested, each one for a one week period, using dynamic off-gas testing to measure the standardised oxygen transfer efficiency (alphaSOTE) . As the DO setpoints were lowered, the total air flow rate to the basin decreased initially . A low DO in the first zones slowed biomass activity and pushed the load towards the end of the aeration basin . The relationship between alphaSOTE and the specific diffuser flow rate qD is different for each zone . In Zone 1 there was a strong decrease in alphaSOTE as qD increased, while Zones 2 and 3 were fairly independent of qD, Zone 2 at a higher level than Zone 3 . Aeration costs were reduced by 15% for the most efficient combination . To achieve even more savings, a control strategy adjusting oxygen transfer rates over the aeration basin to the necessary oxygen transfer rates is suggested . It is based on changing the DO setpoints to reach the lowest total air flow rate while meeting the effluent requirements. Water Sci Technol, 2004, 50(7), 19 - 26 Nutrient removal process development and full scale implementation at the 4 million p.e . main treatment plant of Vienna, Austria; Kroiss H et al.; The Main Treatment Plant of Vienna is in extension for 4 million p.e . and very stringent nutrient removal requirements . The existing high rate BOD removal activated sludge plant (in operation since 1980) is extended by a second stage activated sludge plant and a newly developed flow scheme for nitrogen removal optimisation adaptable to the temperature variations over the year . For this plant pilot investigations have been performed for the development of a specific mathematical model (ASMV) and a specific aeration control strategy . The civil work of the extension is already finished and the installation of the equipment has started . Operation should start in 2004 . The whole project will cost about {see symbol in text}264 million of which about one half is for civil work . The effluent standards correspond to the requirements for sensitive areas in EU Directive for Municipal Waste Water . The raw primary and excess sludge are incinerated after thickening and dewatering . This paper tries to condense the already existing literature with the construction progress and the cost situation. Lett Appl Microbiol, 2004, 39(6), 495 - 503 Isolation and characterization of sulphur-oxidizing Thiomonas sp . and its potential application in biological deodorization; Chen XG et al.; AIMS: To isolate and characterize a sulphur-oxidizing bacterial strain from activated sludge and to evaluate its potential application in biological deodorization . METHODS AND RESULTS: A dominant sulphur-oxidizing bacterial strain, designated as strain SS, was isolated from an enrichment culture using thiosulphate as a sole energy source and CO2 as a sole carbon source . The cells of this organism were aerobic, rod-shaped, Gram-negative and motile . Strain SS could grow autotrophically, heterotrophically as well as mixotrophically . Autotrophic growth was observed at pH values ranging from 2.3 to 9.0 . Phylogenetic analyses revealed that strain SS belonged to Group 1 of the genus Thiomonas, closely related to Thiomonas perometabolis and Thiomonas intermedia . The thiosulphate oxidation rates of strain SS at different pH values were evaluated in terms of oxygen uptake using a Micro-Oxymax respirometer . The results showed that the maximum oxidation rate of 5.65 mg l(-1) h(-1) occurred at 56 h of growth and pH 6.0 . Continuous H2S removal study demonstrated that strain SS could remove more than 99% of H2S when the inlet concentration was below 58.6 ppm . Further increase of the inlet concentration to 118 ppm gave rise to a decline in the removal efficiency to ca 90% . CONCLUSIONS: The strong acidification of the culture medium during the later period could result in the deterioration of the growth activity and the metabolism activity of strain SS . In practical application, the problems caused by the end-product inhibition and the acidification can be alleviated by periodical replacement of culture medium with fresh medium. d, b. Given the physiological flexibility and the ability to remove H2S rapidly and efficiently, strain SS could be a good 'deodorizing' candidate . SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first time that Thiomonas species has been reported for biological deodorization application. Water Sci Technol, 2004, 50(6), 1 - 8 Start up of deammonification process in one single SBR system; Li X et al.; A process for autotrophic nitrogen removal named aerobic/anoxic deammonification wherein NH4+ is oxidized by nearly 50% to NO2- and subsequently the ammonia is converted together with the nitrite to molecular nitrogen (N2 gas), has come to full-scale application within the last few years . In this research, sludge from a biological rotation disk located at a landfill leachate plant at Mechernich, Germany, which is capable of performing the deammonification process, was used as seed sludge for acclimating deammonification activities in laboratory scale batch-reactors . In parallel, the same tests were performed with normal activated sludge . Research results indicated that deammonification activities could be obtained from the seeded reactor and also, with limited performance, from normal activated sludge in a single SBR system after several months acclimation . It was also seen that oxygen is an important factor that influences the deammonification from both the acclimatization process and process running . Further results were approved that report an impact of nitrite as a process intermediate on the closely related process of anaerobic ammonia oxidation ("Anammox") . However, limiting concentrations on a bacteria population performing deammonification were found to be different to those reported for a pure Anammox-culture . Also the influence of another intermediate, hydrazine, was tested for speeding up the acclimating process by inducing the deammonification activities and recovering the activities of deammonification from nitrite inhibition. J Environ Monit, 2004 Nov, 6(11), 855 - 65 Epub 2004 Oct 20. Results of a technology demonstration project to compare rapid aquatic toxicity screening tests in the analysis of industrial effluents; Daniel M et al.; The results of a 'BioWise' demonstration project to assess the comparative sensitivity and practicality of seven new assays for the direct assessment of ecotoxicity in industrial effluents are presented . In addition the aim of the project was to validate the results of the new assays against benchmark data generated from non-proprietary, rapid, microplate screening assays using the regulatory species; freshwater crustacean Daphnia magna and green algae Selenastrum capricornutum, chosen in view of their environmental relevance . The new commercial test assays were: Daphnia magna, Selenastrum capricornutum and Thamnocephalus platyurus Toxkits supplied by Vickers Laboratories Ltd, containing dormant, immobilised life stages of the test species; GreenScreen EM, a yeast based assay for genotoxicity and general acute toxicity supplied by Gentronix Ltd; and CellSense a mediated, amperometric whole cell biosensor based on immobilised activated sludge and E . coli . 38 effluent samples supplied by members of SOCSA (Specialised Organic Chemicals Sector Association) were examined over a period of 13 months, in the project co-ordinated by the AstraZeneca Brixham Environmental Laboratory, and part funded by BioWise via the UK Government Department of Trade and Industry. Microbiology, 2004 Nov, 150(Pt 11), 3741 - 8 Identification and occurrence of tetrad-forming Alphaproteobacteria in anaerobic-aerobic activated sludge processes; Wong MT et al.; In an acetate-fed anaerobic-aerobic membrane bioreactor, a deteriorated enhanced biological phosphorus removal (EBPR) community was developed (as determined based on the chemical profiles of organic substrate, soluble phosphate, and intracellular carbohydrate and polyhydroxyalkanote (PHA) concentrations) . Microscopic observations revealed the dominance of tetrad-forming organisms (TFOs), of which the majority stained positively for PHA under anaerobic conditions . Fluorescence in situ hybridization (FISH) confirmed that the Alphaproteobacteria (85.0+/-7.0% of total cells) were the most dominant group . A 16S rRNA gene clone library specific for the Alphaproteobacteria indicated that most 16S rRNA gene clones (61% of total clones) were closely affiliated with 'Defluvicoccus vanus', forming a cluster within subgroup 1 of the Alphaproteobacteria . Combined PHA staining and FISH with specific probes designed for the members of the 'Defluvicoccus' cluster suggested diversity within this TFO cluster, and that these TFOs were newly identified glycogen-accumulating organisms in EBPR systems . However, these 'Defluvicoccus'-related TFOs were only seen in low abundance in 12 different EBPR and non-EBPR systems, suggesting that they were not the key populations responsible for the deterioration of full-scale EBPR processes. Biochem Biophys Res Commun, 2005 Feb 18, 327(3), 637 - 9 Conceptualizing "suicidal genetically engineered microorganisms" for bioremediation applications; Pandey G et al.; Use of genetically modified microorganisms (GEMs) for pollution abatement has been limited because of risks associated with their release in the environment . Recent developments in the area of recombinant DNA technologies have paved the way for conceptualizing "suicidal genetically engineered microorganisms" (S-GEMS) to minimize such anticipated hazards and to achieve efficient and safer bioremediation of contaminated sites . Our strategy of designing a novel S-GEM is based on the knowledge of killer-anti-killer gene(s) that would be susceptible to programmed cell death after detoxification of any given contaminated site(s). Can J Microbiol, 2004 Sep, 50(9), 697 - 703 Ochrobactrum tritici strain 5bvl1 — characterization of a Cr(VI)-resistant and Cr(VI)-reducing strain; Branco R et al.; Bacterial strain 5bvl1, isolated from a chromium-contaminated wastewater treatment plant and identified as Ochrobactrum tritici, was resistant to a broad range of antibiotics, to Cr(VI), Ni(II), Co(II), Cd(II), and Zn(II), and was able to grow in the presence of 5% NaCl and within the pH range 4–10 . Characterization showed that strain 5bvl1 could be considered a halotolerant and alkalitolerant microorganism resistant to high concentrations of Cr(VI) . This strain was able to grow aerobically in up to 10 mmol.L–1 Cr(VI) . Cr(VI) resistance was independent of sulphate concentration . Under aerobic conditions strain 5bvl1 was also able to reduce high Cr(VI) concentrations (up to 1.7 mmol.L–1) . Increasing concentrations of Cr(VI) in the medium lowered the growth rate of strain 5bv11 but the reduction in growth rate could not be directly correlated with the amount of Cr(VI) reduced . Unlike the type strain, which was only able to reduce Cr(VI), strain 5bvl1 was resistant to Cr(VI) and able to reduce it . Moreover, in strain 5bvl1, the rate and extent of Cr(VI)-reduction were higher than in the other strains of the genus Ochrobactrum . Ochrobactrum strain 5bvl1 resists high Cr(VI) concentrations and has a high Cr(VI)-reducing ability, making it a valuable tool in bioremediation. Chemosphere, 2005 Jan, 58(4), 515 - 22 Bioremediation of a weathered and a recently oil-contaminated soils from Brazil: a comparison study; Trindade PV et al.; The facility with which hydrocarbons can be removed from soils varies inversely with aging of soil samples as a result of weathering . Weathering refers to the result of biological, chemical and physical processes that can affect the type of hydrocarbons that remain in a soil . These processes enhance the sorption of hydrophobic organic contaminants (HOCs) to the soil matrix, decreasing the rate and extent of biodegradation . Additionally, pollutant compounds in high concentrations can more easily affect the microbial population of a recently contaminated soil than in a weathered one, leading to inhibition of the biodegradation process . The present work aimed at comparing the biodegradation efficiencies obtained in a recently oil-contaminated soil (spiked one) from Brazil and an weathered one, contaminated for four years, after the application of bioaugmentation and biostimulation techniques . Both soils were contaminated with 5.4% of total petroleum hydrocarbons (TPHs) and the highest biodegradation efficiency (7.4%) was reached for the weathered contaminated soil . It could be concluded that the low biodegradation efficiencies reached for all conditions tested reflect the treatment difficulty of a weathered soil contaminated with a high crude oil concentration . Moreover, both soils (weathered and recently contaminated) submitted to bioaugmentation and biostimulation techniques presented biodegradation efficiencies approximately twice as higher as the ones without the aforementioned treatment (natural attenuation). Lett Appl Microbiol, 2005, 40(1), 50 - 5 Biodegradation of phenanthrene by the indigenous microbial biomass in a zinc amended soil; Wong KW et al.; Abstract k.w . wong, b.a . toh, y.p . ting and j.p . obbard . 2004.Aims: To study the effect of zinc on the biodegradation of phenanthrene by the microbial biomass in soil . Methods and Results: Uncontaminated soil was amended with zinc and phenanthrene as single or co-contaminants, and microbial metabolic activity was measured using an intracellular dehydrogenase enzyme bioassay over 37 days . Contaminants were amended at optimum, action and double the action level specified in 'The New Dutch List' (Ministry of Housing, Spatial Planning and Environment, the Netherlands, 2000) . Microbial activity in soils with zinc or phenanthrene alone indicated the presence of tolerant, albeit inhibited soil micro-organisms . A zinc concentration at the optimum level of 140 mg kg(-1) in the co-contaminated soil (phenanthrene at 40 mg kg(-1)) resulted in marginal stimulation of the rate of phenanthrene biodegradation . However, Zn(2+) concentrations at the action and double the action level of zinc (720 and 1440 mg kg(-1)) inhibited phenanthrene degradation . Conclusions: Biodegradation of phenanthrene in soils co-contaminated with zinc at concentrations above the action value is impeded . Significance and Impact of the Study: Bioremediation efforts to remove polycyclic aromatic hydrocarbon in zinc co-contaminated soils are likely to be constrained. J Contam Hydrol, 2004 Dec, 75(3-4), 215 - 55 Stable isotope fractionation analysis as a tool to monitor biodegradation in contaminated acquifers; Meckenstock RU et al.; The assessment of biodegradation in contaminated aquifers has become an issue of increasing importance in the recent years . To some extent, this can be related to the acceptance of intrinsic bioremediation or monitored natural attenuation as a means to manage contaminated sites . Among the few existing methods to detect biodegradation in the subsurface, stable isotope fractionation analysis (SIFA) is one of the most promising approaches which is pronounced by the drastically increasing number of applications . This review covers the recent laboratory and field studies assessing biodegradation of contaminants via stable isotope analysis . Stable isotope enrichment factors have been found that vary from no fractionation for dioxygenase reactions converting aromatic hydrocarbons over moderate fractionation by monooxygenase reactions (epsilon=-3 per thousand) and some anaerobic studies on microbial degradation of aromatic hydrocarbons (epsilon=-1.7 per thousand) to larger fractionations by anaerobic dehalogenation reactions of chlorinated solvents (epsilon=between -5 per thousand and -30 per thousand) . The different isotope enrichment factors can be related to the respective biochemical reactions . Based on that knowledge, we discuss under what circumstances SIFA can be used for a qualitative or even a quantitative assessment of biodegradation in the environment . In a steadily increasing number of cases, it was possible to explain biodegradation processes in the field based on isotope enrichment factors obtained from laboratory experiments with pure cultures and measured isotope values from the field . The review will focus on the aerobic and anaerobic degradation of aromatic hydrocarbons and chlorinated solvents as the major contaminants of groundwater . Advances in the instrumental development for stable isotope analysis are only mentioned if it is important for the understanding of the application. J Appl Microbiol, 2005, 98(1), 73 - 83 Biotechnology applied to cultural heritage: biorestoration of frescoes using viable bacterial cells and enzymes; Ranalli G et al.; Abstract g . ranalli, g . alfano, c . belli, g . lustrato, m.p . colombini, i . bonaduce, e . zanardini, p . abbruscato, f . cappitelli and c . sorlini . 2004.Aims: To set up and employ, for the biorestoration of cultural heritage (altered frescoes), an advanced and innovative biotechnology method based on the sequential use of whole viable bacterial cells and specific enzymes . Methods and Results: The bioremediation intervention consisted of the direct application onto an artwork surface of whole bacterial cells of the Pseudomonas stutzeri A29 strain (bioaugmentation), followed by, in a final step, a purified Protease enzyme . The bioremediation was performed on a Spinello Aretino fresco that had become altered by the animal glue residues of past restoration . For the reader's interest the fresco is the 14th century Conversione di S . Efisio e battaglia (Conversion of S . Efisio and battle), size 3.5 x 7.8 m at the Pisa Camposanto Monumentale, Italy . An assessment was made of the final costs of the biological tests (whole bacterial cells, enzymes) so as to compare them with other intervention techniques . Conclusions: A successful innovative biological approach to recover valuable frescoes was set up, and the best conditions for treatment efficiency were identified . Furthermore the cost of the biological cleaning using viable bacterial cells and enzymes (P . stutzeri, Protease, Collagenase, 1 : 3 : 10, ratio respectively) was much lower than that of other conventional methods, making this biotechnology not only very interesting but also very competitive . Significance and Impact of the Study: New biotechnologies with an innovative, soft approach to the 'biocleaning' and 'biorestoration' of cultural heritage are in constant demand, and our results are clear evidence that such an approach has been achieved; the technique could be of significant importance towards developing other goals. Nucleic Acids Res, 2005 Jan 1, 33 Database Issue, D588 - 92 MetaRouter: bioinformatics for bioremediation; Pazos F et al.; Bioremediation, the exploitation of biological catalysts (mostly microorganisms) for removing pollutants from the environment, requires the integration of huge amounts of data from different sources . We have developed MetaRouter, a system for maintaining heterogeneous information related to bioremediation in a framework that allows its query, administration and mining (application of methods for extracting new knowledge) . MetaRouter is an application intended for laboratories working in biodegradation and bioremediation, which need to maintain and consult public and private data, linked internally and with external databases, and to extract new information from it . Among the data-mining features is a program included for locating biodegradative pathways for chemical compounds according to a given set of constraints and requirements . The integration of biodegradation information with the corresponding protein and genome data provides a suitable framework for studying the global properties of the bioremediation network . The system can be accessed and administrated through a web interface . The full-featured system (except administration facilities) is freely available at Additional material: http://www.pdg.cnb.uam.es/biodeg_net/MetaRouter. Biotechnol Lett, 2004 Oct, 26(19), 1497 - 500 Lag period of 14CO2 evolution from dioctyl sulpho{2,3-14C}succinate in relation to adaptation of bacterium, Comamonas terrigena, to dialkyl esters of sulphosuccinate; Godocikova J et al.; Comamonas terrigena, strain N3H, which was isolated from soil polluted with crude oil products, degraded dioctyl sulphosuccinate, a synthetic commercial surfactant . The primary degradation of this compound, the cleavage of ester bonds between octyl groups and sulphosuccinate, lasted significantly shorter time than the subsequent breakdown of the sulphosuccinate moiety of dioctyl sulpho{2,3-(14)C}succinate . (14)CO(2) evolution had a significant shorter lag period with cells in Tris/phosphate medium, without inorganic sulphate and adapted to surfactant, than unadapted cells . The acceleration of the primary degradation by adapted cells also suggest that some enzymes involved in surfactant degradation are inducible . The bacterium may be useful for bioremediation. Arch Microbiol . 2004 Dec 15; {Epub ahead of print} Physiological and molecular genetic analyses of vinyl chloride and ethene biodegradation in Nocardioides sp . strain JS614; Mattes TE et al.; Nocardioides sp . strain JS614 utilizes vinyl chloride and ethene as carbon and energy sources . JS614 could be influential in natural attenuation and biogeochemical ethene cycling, and useful for bioremediation, biocatalysis and metabolic engineering, but a fundamental understanding of the physiological and genetic basis of vinyl chloride and ethene assimilation in strain JS614 is required . Alkene monooxygenase (AkMO) activity was demonstrated in whole-cell assays and epoxyalkane:coenzyme M transferase (EaCoMT) activity was detected in JS614 cell-free extracts . Pulsed-field gel electrophoresis revealed a 290-kb plasmid (pNoc614) in JS614 . Curing experiments and PCR indicated that pNoc614 encodes vinyl chloride/ethene-degradation genes . JS614 vinyl chloride/ethene catabolic genes and flanking DNA (34.8 kb) were retrieved from a fosmid clone . AkMO and EaCoMT genes were found in a putative operon that included CoA transferase, acyl-CoA synthetase, dehydrogenase, and reductase genes . Adjacent to this gene cluster was a divergently transcribed gene cluster that encoded possible coenzyme M biosynthesis enzymes. a, g, i. Reverse transcription-PCR demonstrated the vinyl chloride- and ethene-inducible nature of several genes . Genes encoding possible plasmid conjugation, integration, and partitioning functions were also discovered on the fosmid clone. Environ Pollut, 2005 Mar, 134(2), 301 - 14 Review of disposal technologies for chromated copper arsenate (CCA) treated wood waste, with detailed analyses of thermochemical conversion processes; Helsen L et al.; Several alternative methods for the disposal of chromated copper arsenate (CCA) treated wood waste have been studied in the literature, and these methods are reviewed and compared in this paper . Alternative disposal methods include: recycling and recovery, chemical extraction, bioremediation, electrodialytic remediation and thermal destruction . Thermochemical conversion processes are evaluated in detail based on experiments with model compounds as well as experimental and modelling work with CCA treated wood . The latter category includes: determination of the percentage of arsenic volatilised during thermal conversion of CCA treated wood, identification of the mechanisms responsible for arsenic release, modelling of high temperature equilibrium chemistry involved when CCA treated wood is burned, overview of options available for arsenic capture, characterisation of ash resulting from (co-)combustion of CCA treated wood, concerns about polychlorinated dibenzo-p-dioxins/furans (PCDD/F) formation . Finally, the most appropriate thermochemical disposal technology is identified on short term (co-incineration) and on long term (low-temperature pyrolysis or high-temperature gasification). Appl Microbiol Biotechnol . 2004 Dec 7; {Epub ahead of print} A PCR method for the detection and differentiation of Lentinus edodes and Trametes versicolor in defined-mixed cultures used for wastewater treatment; Garcia-Mena J et al.; A PCR-based method for the quantitative detection of Lentinus edodes and Trametes versicolor, two ligninolytic fungi applied for wastewater treatment and bioremediation, was developed . Genomic DNA was used to optimize a PCR method targeting the conserved copper-binding sequence of laccase genes . The method allowed the quantitative detection and differentiation of these fungi in single and defined-mixed cultures after fractionation of the PCR products by electrophoresis in agarose gels . Amplified products of about 150 bp for L . edodes, and about 200 bp for T . versicolor were purified and cloned . The PCR method showed a linear detection response in the 1.0 mug-1 ng range . The same method was tested with genomic DNA from a third fungus (Phanerochaete chrysosporium), yielding a fragment of about 400 bp . Southern-blot and DNA sequence analysis indicated that a specific PCR product was amplified from each genome, and that these corresponded to sequences of laccase genes . This PCR protocol permits the detection and differentiation of three ligninolytic fungi by amplifying DNA fragments of different sizes using a single pair of primers, without further enzymatic restriction of the PCR products . This method has potential use in the monitoring, evaluation, and improvement of fungal cultures used in wastewater treatment processes. Ground Water, 2004 Nov-Dec, 42(6-7), 880 - 9 Hydraulics of recirculating well pairs for ground water remediation; Cunningham JA et al.; Recirculating well pairs are a proven means of implementing bioremediation and may also be useful for applying other in situ ground water remediation technologies . A bromide tracer test was performed to characterize the hydraulic performance of a recirculating well pair installed at Moffett Field, California . In particular, we estimate two important properties of the recirculating well pair: (1) the fraction of captured water that is recycled between the wells, and (2) the travel-time distribution of ground water in the induced zone of recirculation . We also develop theoretical estimates of these two properties and demonstrate they depend upon a dimensionless pumping rate, denoted xi . The bromide breakthrough curve predicted from theory agrees well with that determined experimentally at Moffett Field . The minimum travel time between the wells is denoted t(min) . In theory, t(min) depends inversely on Q, the pumping rate in the recirculating wells, and is proportional to a2, the square of the distance between the wells . Both the experimental and theoretical travel-time distributions indicate that at least half the recirculating water travels between the wells along fast flowpaths (travel time < 2*t(min)) . Therefore, when designing recirculating well pairs, engineers should ensure that t(min) will be sufficiently high to allow biologically mediated reactions (or other in situ remediation processes) sufficient time to proceed. Arch Biochem Biophys, 2005 Jan 1, 433(1), 176 - 92 The enzymes of oxalate metabolism: unexpected structures and mechanisms; Svedruzic D et al.; Oxalate degrading enzymes have a number of potential applications, including medical diagnosis and treatments for hyperoxaluria and other oxalate-related diseases, the production of transgenic plants for human consumption, and bioremediation of the environment . This review seeks to provide a brief overview of current knowledge regarding the major classes of enzymes and related proteins that are employed in plants, fungi, and bacteria to convert oxalate into CO(2) and/or formate . Not only do these enzymes employ intriguing chemical strategies for cleaving the chemically unreactive C-C bond in oxalate, but they also offer the prospect of providing new insights into the molecular processes that underpin the evolution of biological catalysts. Environ Sci Technol, 2004 Nov 1, 38(21), 5649 - 55 Microbial reduction of U(VI) at the solid-water interface; Jeon OH et al.; Microbial (Geobacter sulfurreducens) reduction of 0.1 mM U(VI) in the presence of synthetic Fe(III) oxides and natural Fe(III) oxide-containing solids was investigated in pH 6.8 artificial groundwater containing 10 mM NaHCO3 . In most experiments, more than 95% of added U(VI) was sorbed to solids, so that U(VI) reduction was governed by reactions at the solid-water interface . The rate and extent of reduction of U(VI) associated with surfaces of synthetic Fe(III) oxides (hydrous ferric oxide, goethite, and hematite) was comparable to that observed during reduction of aqueous U(VI) . In contrast, microbial reduction of U(VI) sorbed to several different natural Fe(III) oxide-containing solids was slower and less extensive compared to synthetic Fe(III) oxide systems . Addition of the electron shuttling agent anthraquinone-2,6-disulfonate (AQDS; 0.1 mM) enhanced the rate and extent of both Fe(III) and U(VI) reduction . These findings suggest that AQDS facilitated electron transfer from G . sulfurreducens to U(VI) associated with surface sites atwhich direct enzymatic reduction was kinetically limited . Our results demonstrate that association of U(VI) with diverse surface sites in natural soils and sediments has the potential to limit the rate and extent of microbial U(VI) reduction and thereby modulate the effectiveness of in situ U(VI) bioremediation. Appl Environ Microbiol, 2004 Dec, 70(12), 7567 - 70 A previously unexposed forest soil microbial community degrades high levels of the pollutant 2,4,6-trichlorophenol; Sanchez MA et al.; 2,4,6-trichlorophenol (2,4,6-TCP) is a hazardous pollutant that is efficiently degraded by some aerobic soil bacterial isolates under laboratory conditions . The degradation of this pollutant in soils and its effect on the soil microbial community are poorly understood . We report here the ability of a previously unexposed forest soil microbiota to degrade high levels of 2,4,6-TCP and describe the changes in the soil microbial community found by terminal restriction fragment length polymorphism (T-RFLP) analysis . After 30 days of incubation, about 50% degradation of this pollutant was observed in soils amended with 50 to 5,000 ppm of 2,4,6-TCP . The T-RFLP analysis showed that the soil bacterial community was essentially unchanged after exposure to up to 500 ppm of 2,4,6-TCP . However, a significant decrease in richness was found with 2,000 and 5,000 ppm of 2,4,6-TCP, even though the removal of this pollutant remained high . The introduction of Ralstonia eutropha JMP134 or R . eutropha MS1, two efficient 2,4,6-TCP degraders, to this soil did not improve degradation of this pollutant, supporting the significant bioremediation potential of this previously unexposed, endogenous forest soil microbial community. Appl Environ Microbiol, 2004 Dec, 70(12), 7558 - 60 Resistance of solid-phase U(VI) to microbial reduction during in situ bioremediation of uranium-contaminated groundwater; Ortiz-Bernad I et al.; Speciation of solid-phase uranium in uranium-contaminated subsurface sediments undergoing uranium bioremediation demonstrated that although microbial reduction of soluble U(VI) readily immobilized uranium as U(IV), a substantial portion of the U(VI) in the aquifer was strongly associated with the sediments and was not microbially reducible . These results have important implications for in situ uranium bioremediation strategies. Appl Environ Microbiol, 2004 Dec, 70(12), 7251 - 9 In situ expression of nifD in Geobacteraceae in subsurface sediments; Holmes DE et al.; In order to determine whether the metabolic state of Geobacteraceae involved in bioremediation of subsurface sediments might be inferred from levels of mRNA for key genes, in situ expression of nifD, a highly conserved gene involved in nitrogen fixation, was investigated . When Geobacter sulfurreducens was grown without a source of fixed nitrogen in chemostats with acetate provided as the limiting electron donor and Fe(III) as the electron acceptor, levels of nifD transcripts were 4 to 5 orders of magnitude higher than in chemostat cultures provided with ammonium . In contrast, the number of transcripts of recA and the 16S rRNA gene were slightly lower in the absence of ammonium . The addition of acetate to organic- and nitrogen-poor subsurface sediments stimulated the growth of Geobacteraceae and Fe(III) reduction, as well as the expression of nifD in Geobacteraceae . Levels of nifD transcripts in Geobacteraceae decreased more than 100-fold within 2 days after the addition of 100 microM ammonium, while levels of recA and total bacterial 16S rRNA in Geobacteraceae remained relatively constant . Ammonium amendments had no effect on rates of Fe(III) reduction in acetate-amended sediments or toluene degradation in petroleum-contaminated sediments, suggesting that other factors, such as the rate that Geobacteraceae could access Fe(III) oxides, limited Fe(III) reduction . These results demonstrate that it is possible to monitor one aspect of the in situ metabolic state of Geobacteraceae species in subsurface sediments via analysis of mRNA levels, which is the first step toward a more global analysis of in situ gene expression related to nutrient status and stress response during bioremediation by Geobacteraceae. Radiats Biol Radioecol, 2004 Sep-Oct, 44(5), 574 - 8 {Isolation and investigation of natural yeast strains resistant to heavy metal salts and radionuclides}; Enzymatic bioremediation: from enzyme discovery to applications; CSIRO Entomology, Canberra, Australian Capital Territory, Australia1 . Enzymatic bioremediation is potentially a rapid method of removing environmental pesticide residues . Applications include the treatment of residues resulting from agricultural production and processing industries, such as the treatment of irrigation waters, surface-contaminated fruit and vegetables and spent dip liquors . 2 . A specific application for some organophosphate-degrading enzymes involves detoxification of nerve agent stockpiles . Effective and affordable remediation requires highly specialized enzymes, so protein engineering techniques are being used to improve properties of various source enzymes to enhance catalytic rates, stability and substrate range . 3 . Trials with an optimized organophosphate-degrading enzyme have shown the feasibility of such technology in various applications . 4 . The enzymes developed for environmental remediation for specific pesticide classes also have applications as antidotes for high-dose pesticide poisonings and as prophylaxis for people at risk of high pesticide doses. Biodegradation, 2004 Dec, 15(6), 435 - 51 Modeling natural attenuation of chlorinated ethenes under spatially varying redox conditions; Widdowson MA; A three-dimensional model for the transport and reductive dechlorination of chlorinated ethenes in ground-water systems with variable redox conditions is demonstrated and applied to a pilot test for accelerated natural attenuation of trichloroethene (TCE) . The rate and extent of biotransformation of TCE and chlorinated progeny is controlled by the dominant terminal electron accepting process (TEAP) that is simulated over space and time . The solute transport code, Sequential Electron Acceptor Model, 3D-transport, (SEAM3D) which simulates aerobic and sequential anaerobic biodegradation of organic carbon, is modified to implement the equations . Results of a generic model for TCE transport in ground-water systems with different redox conditions demonstrate that the degree of chlorinated ethene attenuation is influenced by background concentrations of aqueous- and solid-phase electron acceptors, but that model results are sensitive to other input parameters (inhibition coefficients, maximum rate of reductive dechlorination, biomass concentrations, and ground-water velocity) . Simulation results of enhanced in situ bioremediation using dissolved organic carbon as a reducing agent show that spatial and temporal changes in the dominant TEAP and the subsequent rate of reductive dechlorination are adequately represented with the model . Initial concentrations of Fe(III) and the dechlorinating microbial population influence the simulated time lag observed during the pilot test. Biodegradation, 2004 Dec, 15(6), 419 - 34 Formulation of the CBC-model for modelling the contaminants and footprints in natural attenuation of BTEX; Maurer M et al.; This paper provides the details of the Coupled Biological and Chemical (CBC) model for representing in situ bioremediation of BTEX . The CBC model contains novel features that allow it to comprehensively track the footprints of BTEX bioremediation, even when the fate of those footprints is confounded by abiotic reactions and complex interactions among different kinds of microorganisms . To achieve this comprehensive tracking of all the footprints, the CBC model contains important new biological features and key abiotic reactions . The biological module of the CBC-model includes these important new aspects: (1) it separates BTEX fermentation from methanogenesis, (2) it explicitly includes biomass as a sink for electrons and carbon, (3) it has different growth rates for each biomass type, and (4) it includes inhibition of the different reactions by other electron acceptors and by sulfide toxicants . The chemical module of the CBC-model includes abiotic reactions that affect the footprints of the biological reactions . In particular, the chemical module describes the precipitation/dissolution of CaCO3, Fe2O3, FeS, FeS2, and S degrees . The kinetics for the precipitation/dissolution reactions follow the critical review in Maurer & Rittmann (2004). Biodegradation, 2004 Dec, 15(6), 405 - 17 Modeling intrinsic bioremediation for interpret observable biogeochemical footprints of BTEX biodegradation: the need for fermentation and abiotic chemical processes; Maurer M et al.; The intrinsic bioremediation of BTEX must be documented by the stoichiometric consumption and production of several other compounds, called 'footprints' of the biodegradation reaction . Although footprints of BTEX biodegradation are easy to identify from reaction stoichiometry, they can be confounded by the stepwise nature of the biodegradation reactions and by several abiotic chemical reactions that also produce or consume the footprints . In order to track the footprints for BTEX biodegradation, the following reactions need to be considered explicitly: (1) fermentation and methanogenesis as separate processes, (2) precipitation and dissolution of calcite, (3) precipitation and dissolution of amorphous iron monosulfide (FeS), (4) conversion of FeS into the thermodynamically stable pyrite (FeS2) with loss of sulfide and abiotic formation of H2, and (5) reductive dissolution of solid iron(III) by oxidation of sulfide . We critically review the research that underlies why these mechanisms must be included and how to describe them quantitatively . A companion manuscript develops and applies a mathematical model that includes these reactions. Water Res, 2004 Dec, 38(20), 4405 - 14 Monitoring behaviour of catabolic genes and change of microbial community structures in seawater microcosms during aromatic compound degradation; Sei K et al.; The behaviour of microbial populations responsible for degradation of the aromatic compounds, phenol, benzoate, and salicylate, and changes of microbial community structures in seawater microcosms were analysed quantitatively and qualitatively using MPN-PCR and PCR-DGGE . The purpose of the study was to investigate the ecology of the entire microbial community during bioremediation . Bacterial populations possessing catechol 1,2-dioxygenase (C12O) DNA were evidently the primary degraders of phenol and benzoate, but others possessing catechol 2,3-dioxygenase (C23O) DNA increased to enhance substrate degradation under high-load conditions when the substrates were present for long periods . However, salicylate degradation was evidently facilitated by specific bacterial populations possessing C23O DNA . PCR-DGGE analyses suggested that bacterial populations already relatively dominant in the original microcosm contributed to phenol degradation . Bacteria composing a minor fraction of the original population apparently increased and contributed to benzoate degradation . Bacterial populations possessing C23O DNA were responsible for salicylate degradation, however, and different degrading bacteria were evidently selected for, depending on the initial salicylate concentration . Microbial community structure tended to be simplified by aromatic compound degradation . Thus, microbial monitoring can elucidate the behaviour of bacterial populations responsible for aromatic compound degradation and be used to assess the effects of bioremediation on intact microbial ecosystems. J Appl Microbiol, 2004, 97(6), 1210 - 9 Molecular diversity of tannic acid degrading bacteria isolated from tannery soil; Chowdhury SP et al.; AIMS: The aim of this study was to enrich and isolate bacteria from a tannery soil that were capable of utilizing tannic acid and gallic acid as sole source of carbon aerobically, and to characterize their diversity in order to identify efficient strains that can be used for tannin bioremediation . METHODS AND RESULTS: Bacterial strains were isolated after enrichment in minimal medium with tannic acid or gallic acid as sole carbon source . Polymerase chain reaction (PCR) restricted fragment length polymorphism of 16S rDNA {amplified ribosomal DNA restriction analysis (ARDRA)} and BOX-PCR was used to characterize their diversity . Two strains showing relatively high efficiency in degrading tannic acid and gallic acid were identified on the basis of carbon source utilization pattern (BIOLOG) and 16S rDNA sequence . CONCLUSIONS: Bacterial strains capable of degrading tannic acid and gallic acid could be grouped into six and seven clusters on the basis of ARDRA and BOX-PCR, respectively. i, b, i. On the basis of 16S rDNA sequence, the most efficient isolate degrading tannic acid belonged to Pseudomonas citronellolis, whereas the most efficient gallic acid degrader showed maximum phylogenetic relatedness to P . plecoglossicida . SIGNIFICANCE AND IMPACT OF THE STUDY: Aerobic tannic acid degraders such as the two strains isolated in this study can be used for tannin bioremediation, and in the study of genes involved in the production of tannase, an industrially important enzyme. Mar Pollut Bull, 2004 Nov, 49(9-10), 783 - 8 2,4,6-trinitrotoluene transformation by a tropical marine yeast, Yarrowia lipolytica NCIM 3589; Jain MR et al.; Yarrowia lipolytica NCIM 3589, a tropical marine degrader of hydrocarbons and triglycerides transformed 2,4,6-trinitrotoluene (TNT) very efficiently . Though this yeast could not utilize TNT as the sole carbon or nitrogen source, it was capable of reducing the nitro groups in TNT to aminodinitrotoluene (ADNT) . In a complete medium containing glucose and ammonium sulphate as the available carbon and nitrogen sources respectively, the culture was able to completely transform 1 mM (227 ppm) of TNT under such conditions . A dual pathway was found to be functional, one of which resulted in the formation of the hydride-Meisenheimer complex (H(-)TNT) as a transiently accumulating metabolite that was subsequently denitrated to 2,4-dinitrotoluene (2,4-DNT), whereas the other pathway resulted in the formation of amino derivatives . The presence of increasing amounts of reducing equivalents in the form of glucose promoted better growth and the nitroreductases of this yeast to reduce the aromatic ring to 2,4-DNT although, the reduction of the nitro groups to amino groups was the major functional pathway . The ability of this tropical marine yeast to transform TNT into products such as 2,4-DNT which in turn could be metabolized by other microbes has implications in the use of this yeast for bioremediation of TNT polluted marine environments. Mar Pollut Bull, 2004 Nov, 49(9-10), 740 - 51 Response of the bacterial community to in situ bioremediation of organic-rich sediments; Vezzulli L et al.; A field trial experiment was carried out to assess the potential of bioremediation for mobilisation of carbon in organic-rich sediments . Both bioaugmentation (bio-fixed microorganisms) and biostimulation (oxygen release compounds--ORC) protocols have been tested and the response of the bacterial community has been described to assess the baseline for bioremediation potential . Multifactorial ANOVA revealed that bioaugmentation protocol had an effect in stimulate mobilisation processes and significantly enhanced extra-cellular enzymatic activity rates . In contrast biostimulation treatment did not have an effect on mobilisation rates but contributed to enhance bacterial efficiency through a maximization of the bacterial production:enzymatic activity ratio . Average calculation of net mobilised carbon showed that 23% increase of mobilised pool was accounted for bioaugmentation in summer . Although biostimulation accounted for a smaller increase in mobilised carbon (<10%), the use of ORC resulted in an increased mineralisation and net carbon loss via respiration . Based on our results, a conceptual model for application of bioremediation to face the problem of sediment eutrophication is discussed. Chemosphere, 2005 Jan, 58(1), 83 - 90 Bioremediation potential of a perchlorate-enriched sewage sludge consortium; Bardiya N et al.; The purpose of this work was to explore the reductive bioremediation potential of a perchlorate-enriched facultative anaerobic consortium . Rapid perchlorate reduction and bacterial growth were observed up to 1.84 g l(-1) of perchlorate, but not at 3.82 g l(-1) due to the toxicity . The specific growth rate of the mixed consortium was 0.1 h(-1) . The consortium co-reduced perchlorate and nitrate with acetate as e- donor and carbon source . The presence of nitrate slowed down the perchlorate reduction rate . The other e- acceptors utilized include oxygen, chlorate, Cr(VI), and selenate . Over 95% of the 16 mg l(-1) of added Cr(VI) was reduced within 24 h of incubation with a high-density perchlorate-grown consortium . However, the consortium failed to couple growth with reduction of nitrite, sulfate, thiosulfate, and sulfite . During the search for autotrophic perchlorate reduction, many consortia from very diverse natural sources could not use sulfur compounds such as thiosulfate as e- donor. J Environ Qual, 2005 Jan-Feb, 34(1), 207 - 16 Effect of root death and decay on dissipation of polycyclic aromatic hydrocarbons in the rhizosphere of yellow sweet clover and tall fescue; Parrish ZD et al.; A 12-mo greenhouse study was conducted to evaluate the contribution of root death and decay on the dissipation of polycyclic aromatic hydrocarbons (PAHs) in rhizosphere soil . The contaminated soil was previously treated by land-farming, but residual PAHs remained after treatment . Tall fescue (Festuca arundinacea Schreb.) and yellow sweet clover (Melilotus officinalis Lam.) were the target plants . To specifically evaluate the effect of root decay on contaminant dissipation, plants were treated with glyphosate, a broad spectrum herbicide, to induce root decay . Although tall fescue treatments had the highest root and shoot biomass and root surface area, this plant did not result in the highest contaminant degradation rates . Significant differences were noted between treatments for seven PAHs, with the active yellow sweet clover resulting in 60 to 75% degradation of these compounds . Induced root death and decay did not produce a significant enhancement of PAH degradation . The PAH microbial degrader populations in the vegetated treatments were more than 100 times greater than those in the unvegetated control . The phospholipid fatty acid (PLFA) structural group profile shifted over the growing period, indicating a change in the community structure . In conclusion, phytoremediation was shown to be an effective polishing tool for PAH-affected soil previously subjected to biological treatment. J Hazard Mater, 2005 Jan 31, 117(2-3), 235 - 42 Ozonation of a landfill leachate: evaluation of toxicity removal and biodegradability improvement; Bila DM et al.; This work shows an evaluation of treatments for the leachate produced at the Gramacho Municipal Landfill in Rio de Janeiro state, Brazil . This leachate has very peculiar characteristics, with a high salinity level and very low biodegradability (BOD(5)/COD of 0.05) . A sequence of processes was employed in the treatment of this leachate . Initially, a physicochemical treatment was used, while the second stage consisted of application of ozone to improve the biodegradability of the leachate . The final stage comprised a biological treatment . The physical-chemical treatment led to COD and DOC removal levels of 40 and 25%, respectively, with the use of Al(2)(SO(4))(3) . The sequence of treatments proposed brought good results, with an increase in the BOD(5)/COD ratio from 0.05 to 0.3 after ozonation . The toxicity tests performed using Brachydanio rerio and Poecilia vivipara showed that the toxicity of the leachate had hardly been reduced by ozonation . These results are in agreement with the fact that, despite the higher BOD(5)/COD ratio, the biological process did not present a good performance . The total average removal levels of COD and DOC achieved using the combined treatment were 73 and 63%, respectively, for an ozone dose of 3.0gL(-1) by the leachate. Biotechnol Bioeng . 2004 Dec 29; {Epub ahead of print} Effects of pH amendment on metal working fluid wastewater biological treatment using a defined bacterial consortium; van der Gast CJ et al.; The aim of this study was to determine whether pH amendment of a highly alkaline metal working fluid (MWF) wastewater would improve biological treatment in a bioreactor system following introduction of a bacterial inoculum (comprised of the following strains: Agrobacterium radiobacter, Comamonas testosteroni, Methylobacterium mesophilicum, Microbacterium esteraromaticum, and Microbacterium saperdae) . The pH values tested were 6, 7, 8, and 9 . Three replicate batch mode bioreactors inoculated with the bacterial inoculum (plus an abiotic control bioreactor) were operated for each of the four pH conditions . After 14 days, the final mean chemical oxygen demand (COD) reduction at pH 9 was 50 +/- 1.4%; at pH 8, 58 +/- 1.4%; pH 7, 65 +/- 1.0%; and pH 6, 75 +/- 2.7% of the initial COD (approximately 10,000 mg L(-1)), respectively . Interestingly, within 5 days, the pH in all inoculated bioreactors progressed toward pH 8 . However, all abiotic control bioreactors remained at the pH at which they were amended . The fate of the inoculum, determined by denaturing gradient gel electrophoresis (DGGE) and by cluster analysis of the resulting DGGE profiles, revealed that the inocula survived throughout operation of all pH-amended bioreactors . Length-heterogeneity polymerase chain reaction (PCR) was used to track the population dynamics of individual strains . After 7 days of operation, M . esteraromaticum was the most abundant population in all bioreactors, regardless of pH . From our findings, it appears necessary to adjust the MWF wastewater from pH 9 to between 6 and 7, to achieve optimal biological treatment rates . (c) 2004 Wiley Periodicals, Inc. Nutr Health, 2004, 18(1), 3 - 27 From superior adaptation and function to brain dysfunction--the neglect of epigenetic factors; Saugstad LF; With optimal pregnancy conditions (natural, enriched diet which includes fish) African (Digo) infants are 3-4 weeks ahead of European/American infants in sensorimotor terms at birth, and during the first year . Infants of semi-aquatic sea-gypsies swim before they walk, and have superior visual acuity compared with us . With adverse pregnancy behaviour (fear of fat, a trend to dieting), neglecting the need for brain fat to secure normal brain development and function, we run a risk of dysfunction--death . Sudden Infant Death Syndrome victims have depressed birth weight, lower levels of marine fat in brainstem than controls, and >80 suffer multiple hypoxic episodes prior to death . Depressed birth weight (more than 10% below mean) is seen in learning and behaviour disorders, and a trend towards weights of less than 3kg is increasing, which supports a rise in antenatal sub optimality . Given marine fat deficiency in pregnancy and infancy, neurons starved for fuel could delay myelination and maturation in the latest developed Frontal Lobes . The phylogenetic oldest Lateral Frontal Lobe System (feed-back mechanism etc.) derived from olfactory bulb-amygdala, which crosses in Anterior Commisure is probably spared, while the Medial Frontal Lobe System derived from Hippocampus-Cingulum and crosses in Corpus Callosum (delayed response task) is most likely affected . The rise in infantile autism (intact vision and hearing) with deficit in delayed response task only, could suggest a deficit in the Medial Frontal Lobe System . The human species is unique; 70% of total energy to the foetus goes to development of the brain, which mainly consists of marine fat . It undergoes pervasive regressive events, before birth, in infancy and at puberty . Minimal retraction of neuronal arborisation is advantageous . Attributable to adverse pregnancy childrearing practice, excessive retraction is likely prenatally and in infancy . Pubertal age affects the fundamental property of nervous tissue, excitability: excessive excitatory drive is seen in early, and a deficiency in late puberty . It is postulated that with adequate marine fat, there is probably no risk of psychopathology at the extremes, whereas a deficiency could lead to paroxysmal (subcortical) dysfunction in early puberty, and breakdown of cortical circuitry and cognitive dysfunctions in late puberty . The post-pubertal psychoses, schizophrenia and manic-depressive psychosis at the extremes of the pubertal age continuum, with contrasting excitability and biological treatment, are probably the result of continuous dietary deficiency, which has inactivated the expression of genes for myelin development and oligodendrocyte-related genes in their production of myelin . The beneficial effect of marine fat in both disorders, in other CNS disorders as well as in developmental dyslexia (DD) and ADHD among others, supports our usual diet is persistently deficient . We have neglected the similarity of our great brain to other mammals, and our marine heritage . Given the amount of marine fat needed to secure normal brain development and function is not known, nor the present dietary level, it seems unduly conjectural to postulate that a dietary deficiency in marine fat is causing brain dysfunction and death . However, all observations point in the same direction: our diet focusing on protein mainly, is deficient, the deficiency is most pronounced in maternal nutrition and in infancy. Water Res, 2004 Dec, 38(20), 4331 - 40 Potentials of biological oxidation processes for the treatment of spent sulfidic caustics containing thiols; Sipma J et al.; This research focused on the biological treatment of sulfidic spent caustics from refineries, which contain mainly hydrogen sulfide, methanethiol (MT) and ethanethiol (ET) . Also various organic compounds can be present such as BTEX . Biological oxidation of 2.5 mM MT in batch experiments occurred after MT was first auto-oxidized into dimethyldisulfide (DMDS) whereafter oxidation into sulfate was completed in 350 h . DMDS as sole substrate was completely oxidized within 40 h . Therefore, DMDS formation seems to play an important role in detoxification of MT . Biological oxidation of ET and buthanethiol was not successful in batch experiments . Complete oxidation of MT and ET was observed in flow-through reactor experiments . Simultaneous oxidation of sulfide and MT was achieved when treating a synthetic spent caustic, containing 10 mM sulfide and 2.5 mM MT, in a bubble column reactor with carrier material at a hydraulic retention time of 6 h . Addition of 7.5 mM phenol, a common pollutant of spent caustics, did not adversely affect the biological oxidation process and phenol was completely removed from the effluent . Finally, three different spent caustics solutions from refineries were successfully treated. Water Sci Technol, 2004, 50(7), 49 - 52 Combined quantity management and biological treatment of sludge liquor at Hamburg's wastewater treatment plants--first experience in operation with the Store and Treat process; Laurich F; Store and Treat (SAT) is a new concept for the management of ammonium-rich process waste waters at wastewater treatment plants . It combines the advantages of quantity management and separate biological treatment, whereby both operations are carried out in the same tank . Now the first full-scale application of that method was realized in Hamburg . As first experience shows the process can help to increase nitrogen removal and to reduce energy consumption. Environ Sci Technol, 2004 Oct 15, 38(20), 5470 - 5 Electrochemical oxidation as a final treatment of synthetic tannery wastewater; Panizza M et al.; Vegetable tannery wastewaters contain high concentrations of organics and other chemicals that inhibit the activity of microorganisms during biological oxidations, so biorefractory organics that are not removed by biological treatment must be eliminated by a tertiary or advanced wastewater treatment . In this paper, the applicability of electrochemical oxidation as a tertiary treatment of a vegetable tannery wastewater was investigated by performing galvanostatic electrolysis using lead dioxide (Ti/PbO2) and mixed titanium and ruthenium oxide (Ti/TiRuO2) as anodes under different experimental conditions . The experimental results showed that both the electrodes performed complete mineralization of the wastewater . In particular, the oxidation took place on the PbO2 anode by direct electron transfer and indirect oxidation mediated by active chlorine, while it occurred on the Ti/TiRuO2 anode only by indirect oxidation . Furthermore, the Ti/PbO2 gave a somewhat higher oxidation rate than that observed for the Ti/TiRuO2 anode . Although the Ti/TiRuO2 required almost the same energy consumption for complete COD removal, it was more stable and did not release toxic ions, so it was the best candidate for industrial applications . With the Ti/TiRuO2 anode, the rate of tannery wastewater oxidation increased with the current density, pH, and temperature of the solution . These results strongly indicate that electrochemical methods can be applied effectively as a final treatment of vegetable tannery wastewater allowing the complete removal of COD, tannin, and ammonium and decolorization. Water Sci Technol, 2004, 50(6), 69 - 78 Biological nutrient removal model No.1 (BNRM1); Seco A et al.; This paper presents the results of the work carried out by the CALAGUA Group on Mathematical Modelling of Biological Treatment Processes: the Biological Nutrient Removal Model No.1 . This model is based on a new concept for dynamic simulation of wastewater treatment plants: a unique model can be used to design, simulate and optimize the whole plant, as it includes most of the biological and physico-chemical processes taking place in all treatment operations . The physical processes included are: settling and clarification processes (flocculated settling, hindered settling and thickening), volatile fatty acids elutriation and gas-liquid transfer . The chemical interactions included comprise acid-base processes, where equilibrium conditions are assumed . The biological processes included are: organic matter, nitrogen and phosphorus removal; acidogenesis, acetogenesis and methanogenesis . Environmental conditions in each operation unit (aerobic, anoxic or anaerobic) will determine which bacterial groups can grow . Thus, only the model parameters related to bacterial groups able to grow in any of the operation units of a specific WWTP will require calibration . One of the most important advantages of this model is that no additional analysis with respect to ASM2d is required for wastewater characterization . Some applications of this model have also been briefly explained in this paper. Water Sci Technol, 2004, 50(5), 329 - 34 Comparison of different advanced oxidation process to reduce toxicity and mineralisation of tannery wastewater; Schrank SG et al.; Many organic compounds contained in wastewater are resistant to conventional chemical and/or biological treatment . Because of this reason different degradation techniques are studied as an alternative to biological and classical physico-chemical processes . Advanced Oxidation Processes (AOPs) probably have developed to become the best options in the near future . AOP while making use of different reaction systems, are all characterised by the same chemical feature: production of OH radicals (*OH) . The versatility of AOPs is also enhanced by the fact that they offer different possibilities for OH radical production, thus allowing them to conform to specific treatment requirements . The main problem with AOPs is their high cost . The application of solar technologies to these processes could help to diminish that problem by reducing the energy consumption required for generating UV radiation . In this work, different AOPs (O3, TiO2/UV, Fenton and H2O2/UV) were examined to treat tannery wastewater or as a pre-treatment step for improving the biodegradation of tannery wastewater, at different pH and dosage of the chemicals . Under certain circumstances retardation in biodegradation and/or an increase in toxicity may be observed within these treatment steps . Two different bioassays (Daphnia magna and Vibrio fischeri) have been used for testing the progress of toxicity during the treatment . In parallel other objectives were to analyse and identify organic compounds present in the untreated wastewater and arising degradation products in AOP treated wastewater samples. f, g, j, b. For this purpose substance specific techniques, e.g., gas chromatography-mass spectrometry (GC-MS) in positive electron impact (El(+)) mode and atmospheric pressure ionisation (API) in combination with flow injection analysis (FIA) or liquid chromatography-mass and tandem mass spectrometry (LC-MS or LC-MS-MS) were performed. Biosens Bioelectron, 2004 Oct 15, 20(3), 571 - 8 Short-term BOD (BODst) as a parameter for on-line monitoring of biological treatment process; Part II: instrumentation of integrated flow injection analysis (FIA) system for BODst estimation; Liu J et al.; An instrument with integrated flow injection analysis (FIA) system has been developed for on-line monitoring a process for conversion of biomass under field condition . The instrument consists of a newly designed biosensor for easy renewal of the bio-receptor without disassembling the sensor, a FIA controller for controlling the analysis operations, and a computer-based data acquisition system for data recording and processing . The instrument performed a sequence operations automatically including preparation of sample in the desired concentration, sample loading, sample injection, signal recording, data processing, and self-cleaning of the system . This makes the instrument being an interesting and promising device for on-line process monitoring. Biosens Bioelectron, 2004 Oct 15, 20(3), 562 - 70 Short-term BOD (BODst) as a parameter for on-line monitoring of biological treatment process . Part I . A novel design of BOD biosensor for easy renewal of bio-receptor; Liu J et al.; A novel design of a biochemical oxygen demand (BOD) biosensor has been developed for on-line monitoring of easily biodegradable organic compounds in aqueous samples . The biological recognition element of the sensor could be easily renewed by injecting new bacterial paste without disassembling the sensor system . The sensor measurements were carried out in the initial-rate mode using a flow injection (FI) system, resulting in 60 s for one sample analysis followed by a recovery time less than 10 min . The sensor performance achieved showed a wide detection linearity over the range of 5-700 mg BOD5.l(-1) and a generally good agreement between the BOD values estimated by the biosensor and the conventional 5-day test . Furthermore, the precision test was in the control range (i.e . repeatability < or = /+/-7.5%/, reproducibility < or = /+/-7.3%/) . The sensor could be used over 1 week in continuous test, however, the best performance was found within the first 24 h where standard deviation of the sensor response was +/-2.4% . The design of the sensor allows easy and fast renewal of the cells used as sensing elements . Replacement of biological recognition element and calibration of the sensor responses can be performed in a rather simple procedure on a daily regular basis . By using a mixed culture as the bio-receptor, one gets a sensor that reacts to a wide range of substrates . The new sensor construction will thus allow fast and convenient replacement of the bio-receptor and on-line assay of a broad range of substrates . This makes the sensor being an interesting and promising candidate for on-line monitoring of biological treatment process. Water Res, 2004 Nov, 38(19), 4186 - 96 Chemical characterisation of natural organic substrates for biological mitigation of acid mine drainage; Gibert O et al.; The current approach of the biological treatment of acid mine drainage by means of a passive remediation system involves the choice of an appropriate organic substrate as electron donor for sulphate reducers . Nowadays this selection is one of the critical steps in the performance of such treatment, as this depends to a great extent on the degradability of the organic substrate . Thus, a prior characterisation of the organic substrate predicting its biodegradability would be desirable before embarking on an extensive large-scale application . The aim of this study was to correlate the chemical composition (lignin content) of four different natural organic substrates (compost, sheep and poultry manures, oak leaf) and their capacity to sustain bacterial activity in an attempt to predict biodegradation from chemical characterisation . The results showed that the lower the content of lignin in the organic substrate, the higher its biodegradability and capacity for developing bacterial activity . Of the four organic materials, sheep and poultry manures and oak leaf evolved reducing conditions and sustained active sulphidogenesis, which coupled with the decrease in sulphate concentration indicated bacterial activity . Sheep manure was clearly the most successful organic material as electron donor (sulphate removal >99%), followed by poultry manure and oak leaf (sulphate removal of 80%) . Compost appeared to be too poor in carbon to promote sulphate-reducing bacteria activity by itself . Column experiments emphasised the importance of considering the residence time as a key factor in the performance of continuous systems . With a residence time of 0.73 days, sheep manure did not promote sulphidogenesis . However, extending residence time to 2.4 and 9.0 days resulted in an increase in the sulphate removal to 18% and 27%, respectively. J Environ Sci Health A Tox Hazard Subst Environ Eng, 2004 Aug, 39(9), 2391 - 404 Landfill leachate treatment by yeast and bacteria based membrane bioreactors; Wichitsathian B et al.; Biological treatment of medium-age landfill leachate was investigated on a membrane bioreactor . The experiments were conducted in two 5-L reactors with immersed hollow fiber microfiltration membranes . One reactor was operated with a mixed bacterial culture termed as bacteria based membrane bioreactor (BMBR) while the other with mixed yeast culture termed as yeast based membrane bioreactor (YMBR) . The leachate was characterized with a chemical oxygen demand (COD) concentration of 7000-9000mg/L, biochemical oxygen demand (5 days) to chemical oxygen demand ratio (BOD5/COD) of 0.35-0.45 and total Kjeldahl nitrogen (TKN) of 1800-2000mg/L . The performance was assessed with and without ammonia stripping . In both the reactors, the average COD and TKN removal efficiency without ammonia stripping ranged between 52-66 and 14-28%, respectively . The performance of both the membrane bioreactors improved with ammonia stripping in terms of both COD (72-76%) and TKN (82-89%) removal efficiency . Though, the difference in the performance of the BMBR and YMBR was not significant in terms of COD removal, the YMBR showed better removal efficiency in terms of BOD5 . The molecular weight cut-off showed that the degradation pathway of the leachate by bacterial and yeast are different . In regard to membrane fouling, the YMBR showed better performance with lower trans-membrane pressure as well as longer operating time . This superior performance of the YMBR could be due to the structure of yeast cells which are larger in size as well as reduced soluble extracellular polymeric substances (EPS) production, which are the main cause of membrane biofouling. Curr Opin Biotechnol, 2004 Oct, 15(5), 463 - 8 Membrane bioreactors for the removal of anionic micropollutants from drinking water; Crespo JG et al.; Biological treatment processes allow for the effective elimination of anionic micropollutants from drinking water . However, special technologies have to be implemented to eliminate the target pollutants without changing water quality, either by adding new pollutants or removing essential water components . Some innovative technologies that combine the use of membranes with the biological degradation of ionic micropollutants in order to minimize the secondary contamination of treated water include pressure-driven membrane bioreactors, gas-transfer membrane bioreactors and ion exchange membrane bioreactors. Water Sci Technol, 2004, 50(3), 195 - 206 Biological treatment of whitewater in a laboratory process in order to determine kinetic parameters for model development; Alexandersson T et al.; Implementation of an in-mill biological treatment plant is one solution to the problems associated with closure of whitewater systems . It is, however, important to operate the treatment with low concentration of nutrients in the effluent . The effect on the COD reduction from decreased additions of NH4-N and PO4-P were investigated in three parallel aerobic suspended carrier reactors during treatment at 46 to 48 degrees C of whitewater from a recycled paper mill producing liner and fluting . In the reference reactor, a COD reduction of 89% was achieved and 45.6 mg NH4-N/(g COD reduced) and 11.6 mg PO4-P/(g COD reduced) was consumed at an organic load around 20 kg COD/(m3 x d) . Reduced additions of NH4-N decreased the COD reduction . Addition of 56% of the consumption of NH4-N in the reference reactor resulted in a COD reduction of 80% . The response from decreased addition of PO4-P was different compared to NH4-N but it could not be determined if this is due to unsuitable experimental design or a different reaction mechanism . Reducing the addition of PO4-P to 26% of the consumption of PO4-P in the reference reactor, decreased the COD reduction to 83% . The main conclusion from the experiment is: biological treatment has the potential of treating whitewater from recycled paper mills with low effluent nutrient concentrations. Water Sci Technol, 2004, 50(3), 183 - 94 Pulp mill process closure: a review of global technology developments and mill experiences in the 1990s; Stratton SC et al.; The impact of effluent discharges continues to be an important issue for the pulp manufacturing industry . Considerable progress has been made in pollution prevention to minimize waste generation, so-called manufacturing "process closure." Since the mid-1980s many important technologies have been developed and implemented, many of these in response to organochlorine concerns . Zero effluent operation is now a reality for a few bleached chemi-thermomechanical pulp (BCTMP) pulp mills . In kraft pulp manufacturing, important developments include widespread adoption of new cooking techniques, oxygen delignification, closed screening, improved process control, new bleaching methods, and systems that minimize pulping liquor losses . Coupled to this is a commitment to reduce water use and maximize reuse of in-mill process streams . Some companies pursued bleach plant closure, and many have been successful in eliminating a portion of their bleaching wastewaters . However, the difficulties inherent in closing bleach plants are considerable . For many mills the optimal solution has been found to be a high degree of closure coupled with external biological treatment of the remaining process effluent . No bleach plants at papergrade bleached kraft mills are known to be operating effluent-free on a continuous basis . This paper reviews the important worldwide technological developments and mill experiences in the 1990s that were focused on minimizing environmental impacts of pulp manufacturing operations. Water Sci Technol, 2004, 50(3), 145 - 56 Integrated biological treatment of recalcitrant effluents from pulp mills; Ortega-Clemente A et al.; This work aimed at determining the degree of depuration of a recalcitrant effluent (weak black liquor, WBL) achieved in a series treatment consisting of a first stage methanogenic fluidised bed reactor followed by a second stage aerobic, upflow reactor packed with "biocubes" of Trametes versicolor immobilised onto small cubes of holm oak wood . The mesophilic, lab scale methanogenic fluidised bed reactor contained a microbial consortium immobilised onto granular activated carbon 500 microm average size . The process removed decreasing amounts of organic matter at decreasing hydraulic retention times (HRT), eventually reaching an average of 50% at 0.5 day HRT . Colour and ligninoid removals also decreased with decreasing HRT . Although the methanogenic fluidised bed reactor provided an effective treatment for the degradable organic matter, important concentrations of recalcitrant organic matter and colour still remained in the anaerobic effluent . This anaerobic effluent was fed to the aerobic packed bed reactor . Two HRT were tested in this unit, namely 5 and 2.5 days . The reactor averaged an organic matter removal in the range of 32% COD basis, during an experimental run of 95 days . Colour and ligninoid contents were removed in high percentages (69% and 54%, respectively) . There was no significant difference in reactor performance at 5- and 2.5-day HRT . There was a positive correlation between pollutant removal efficiencies and Laccase activity in crude extracts of the reactor liquor . No supplemental soluble carbohydrate was required to sustain the fungus activity and the consistent reactor performance . Overall, the two-stage treatment achieved approximately a 78% removal of the original organic matter of the WBL (COD basis) and ca . 75% of colour and ligninoid contents. Rev Iberoam Micol, 2003 Dec, 20(4), 164 - 8 {Treatment of coloured industrial effluents with Pleurotus spp}; Rodriguez S et al.; The decolouration of fermentation residues (vinasse) and liquid extract of coffee pulp by the mushroom Pleurotus ostreatus was studied in addition to laccase activity . The fungus was inhibited in both residues when they remained undiluted . In submerged cultivation on wastewaters a good production of biomass (14.8 g/l for vinasse and 5.4 g/l for extract of coffee pulp) and also laccase activity (14.1 U/ml for vinasse and 3.0 U/ml for extract of coffee pulp) up to the 10 days of fermentation was observed, being significantly greater in the culture with vinasse . It was shown that treatment with this mushroom reduces both the chemical oxygen demand and the colour, contributing to their biological treatment. Waste Manag, 2004, 24(8), 775 - 83 Biostabilization of municipal solid waste; Adani F et al.; A mechanical-biological process for municipal solid waste (MSW) treatment was monitored for one year . Mechanical pre-treatment provided two fractions . The oversize fraction (diameter > 50 mm) (yield of 600 g kg(-1) ww) (46 Mg day(-1)) was used for refuse derived fuel production, after undergoing a mechanical refining processes, because of low moisture content (200-250 g kg(-1)) and high calorific value (2500-2800 kcal kg ww(-1)) . The undersize fraction (diameter < 50 mm) (yield 400 g kg(-1) ww) (30 Mg day(-1)) contained about 800 g kg(-1) of the MSW organic matter . This fraction was biologically treated using an aerobic process with an organic waste fraction from separate collection (77 Mg day(-1)) and recycled stabilized material (62 Mg day(-1)) obtained from end-product sieve (diameter < 20 mm) used as bulking agent . A retention time of three weeks was sufficient to obtain stabilized products in agreement with up-dated rules of the Lombardy Region (North Italy) regarding biostabilization and composting processes . Dynamic Respiration Index (DRI), such as required by both Lombardy Region rules and suggested by the European Community, was chosen in preference to other indices in order to assess the degree of biological stability of the end products . A mean DRI value of 1164 mg O2 kg SV(-1) h(-1) was obtained and is in agreement with the proposed limit of 1000+/-200 mg O2 kg SV(-1) h(-1) . Self-heating test, potential biogas production and fermentable volatile solids were also used as parameters to describe the potential impact of treated waste, providing further useful information . Nevertheless, all of these methods revealed analytical or interpretative limits . A complete mass balance of the biological treatment section showed that, from a net input of 107 Mg day(-1), only 250 g kg(-1) (27 Mg day(-1)) of the waste needed to be landfilled, with 750 g kg(-1) (80 Mg day(-1)) being lost as CO2 and H2O. J Biotechnol, 2004 Sep 30, 113(1-3), 321 - 6 Metal solubilization from metal-containing solid materials by cyanogenic Chromobacterium violaceum; Faramarzi MA et al.; Different cyanogenic bacterial strains (Chromobacterium violaceum, Pseudomonas fluorescens, Bacillus megaterium) were cultivated under cyanide-forming conditions in the presence of metal-containing solids such as nickel powder or electronic scrap . All microorganisms were able to form water-soluble metal cyanides, however, with different efficiencies . C . violaceum was able to mobilize nickel as tetracyanonickelate {Ni(CN)4(2-)} from fine-grained nickel powder . Gold was microbially solubilized as dicyanaoaurate {Au(CN)2-} from electronic waste . Additionally, cyanide-complexed copper was detected during biological treatment of shredded printed circuit boards scrap . Regarding the formation of tetracyanonickelate, C . violaceum was more effective than P . fluorescens or B . megaterium . Besides a few previous reports on gold solubilization from gold-containing ores or native gold by C . violaceum, the findings demonstrate for the first time the microbial mobilization of metals other than gold from solid materials and represent a novel type of microbial metal mobilization based on the ability of certain microbes to form HCN . The results might have the potential for industrial applications (biorecovery, bioremediation) regarding the treatment of metal-containing solids since metal cyanides can easily be separated by chromatographic means and be recovered by sorption onto activated carbon. J Biotechnol, 2004 Sep 30, 113(1-3), 295 - 304 How to avoid pharmaceuticals in the aquatic environment; Larsen TA et al.; Pharmaceuticals and other micropollutants in wastewater pose a new challenge to wastewater professionals as well as to the pharmaceutical industry . Although there is a great deal of uncertainty concerning the possible detrimental effects on the aquatic ecosystems, the precautionary principle--or possibly new scientific evidence--may give rise to more stringent demands on wastewater treatment in the future . In conventional wastewater treatment plants, a combination of biological treatment with high sludge residence times and ozonation of the effluent seems to be the most promising technology . Ozonation, however, is an energy-intensive technology . Moreover, in conventional end-of-pipe systems a large part of the pollutants will always be lost to the environment due to leaking, primarily during rain . In the long term, source separation offers the more sustainable solution to the entire wastewater problem, including organic micropollutants . Urine source separation is an elegant solution to the problems of nutrients and pharmaceuticals alike and losses of untreated pollutants to the environment can be minimized . Although few technologies for the separate treatment of urine have been developed to date, the 100-500 times higher concentrations of micropollutants promise more efficient conditions for all removal technologies known from conventional wastewater treatment. Environ Toxicol Chem, 2004 Sep, 23(9), 2049 - 60 Fate and stability of 14C-labeled 2,4,6-trinitrotoluene in contaminated soil following microbial bioremediation processes; Weiss M et al.; Biological treatment of 2,4,6-trinitrotoluene (TNT) in soil rarely results in complete mineralization of the parent compound . More often, the largest proportion of the TNT carbon is incorporated into the soil organic matrix . Therefore, we evaluated the stability of nonextractable residues from various bioremediation processes of 14C-TNT in soils . The extractable amounts of the residual radioactivity varied between 7 and 33% and thus the nonextractable amount between 93 and 67% (3-15% in fulvic acids, 26-46% in humic acids, and 27-44% in the humin fraction) . The residue-containing soils were analyzed for the release of radioactivity after treatment by physical (freeze and thaw, grinding of soil, and steam extraction), chemical (acid rain and addition of metal complexing agent), and biological methods (addition of compost, white rot fungi, radical-generating enzymes, and germination of plants) . Freeze and thaw treatment and grinding of the soil did not alter the partitioning of the label significantly . Steam extraction and acid rain extraction increased the water extractability to 11 to 29% and to 51.6% in the native TNT-contaminated soil . The addition of ethylenediamine-tetraacetate (EDTA) increased the extractability from 7 to 12%. d, h, a, c, j, b. After biological treatment, only slightly increased extractability (<10%) was observed . No increase of extractable TNT or known metabolites was observed with any of the treatments . Thus, under the treatment conditions applied in this study, the residues formed during microbial transformation of TNT may be biogenic residues with low mobilization potential and low hazardous impact. Bioresour Technol, 2005 Jan, 96(1), 55 - 8 Biotreatment of wastewater using aquatic invertebrates, Daphnia magna and Paramecium caudatum; Shiny KJ et al.; A number of major changes have occurred over the past few years, which give cause for a re-examination of conventional wastewater treatment methods . Among these are growing problems of worldwide energy and food shortages and nutrients not removed by conventional secondary processes causing algal blooms and other problems in the receiving waters . The global increase in wastewater calls for innovative low cost technology approaches to its recycling . Biotreatment systems, utilizing living organisms are receiving growing attention since they are ecologically sound, cheap and applicable in areas without land constraints . Filter feeders (both invertebrates and vertebrates) are promising in this area since they can remove suspended organic matter and bacteria, even in the size range of microns . In the present study biological treatment of municipal wastewater using two invertebrates--Paramecium caudatum, a protozoan and Daphnia magna, a cladoceran was investigated . Analysis at pre-experimental and post-experimental stages revealed the potential of these species in abatement of water pollution . D . magna was more efficient than P . caudatum in laboratory-scale studies. Environ Technol, 2004 Jul, 25(7), 801 - 7 Fe(III)-EDTA complex abatement using a catechol driven Fenton reaction combined with a biological treatment; Oviedo C et al.; A combined chemical oxidation (catechol-driven Fenton reaction) followed by a biological treatment was used to degrade Fe(III)-EDTA (1.34 mM) . The chemical treatment was inspired in fungal non-enzymatic wood rot mechanisms that use dihydroxybenzens in order to promote the Fenton reaction to breakdown wood structures . This chemical pre-oxidation used catechol (50 microM) and H202 (20 mM) and the reaction products were identified by GC-MS . In addition, a biological treatment was coupled using the baker's yeast Saccharomyces cerevisiae . The combined chemical biological treatment achieved 100% EDTA degradation, 68 % total organic carbon removal and 90% iron removal. World J Biol Psychiatry, 2004 Jul, 5(3), 120 - 35 The World Federation of Societies of Biological Psychiatry (WFSBP) guidelines for the biological treatment of bipolar disorders, part III: maintenance treatment; Grunze H et al.; As with the two preceding guidelines of this series, these practice guidelines for the pharmacological maintenance treatment of bipolar disorder were developed by an international task force of the World Federation of Societies of Biological Psychiatry (WFSBP) . Their purpose is to supply a systematic overview of all scientific evidence relating to maintenance treatment . The data used for these guidelines were extracted from a MEDLINE and EMBASE search, from recent proceedings from key conferences and various national and international treatment guidelines . The scientific justification of support for particular treatments was categorised into four levels of evidence (A-D) . As these guidelines are intended for clinical use, the scientific evidence was not only graded, but also reviewed by the experts of the task force to ensure practicality. Water Sci Technol, 2004, 50(1), 253 - 7 Evaluation of virological quality of sewage from four biological treatment plants by a nested-PCR technique; Komninou G et al.; In order to determine the virological quality of sewage from four biological treatment plants in Greece (two in the city of Athens and two in the city of Patras), 92 raw sewage samples were analysed for the presence of enteroviruses and adenoviruses during the period from October 2000 to February 2003 . A nested-PCR method was used in order to increase the sensitivity of virus detection . Enteroviruses were detected in 43 samples (47%) and adenoviruses in 75 samples (81.5%) of raw sewage by nested PCR . The more frequent isolation of adenoviruses in raw sewage indicated their stability as virological indicators of the pollution of the environment and their increased persistence in sewage. J Air Waste Manag Assoc, 2004 Dec, 54(12), 1534 - 42 Hydration properties of eco-cement pastes from waste sludge ash clinkers; Lin KL et al.; Three types of hydraulic cements have been developed by incorporating sludge ash from a primary sewage treatment plant and a water purification plant, as well as slag from steelworks (ferrate), as a partial replacement for clay, silica, alumina, and iron oxide in raw cement meal . The raw meal for the pre-determined recipes was prepared by heating it to 1400 degrees C for 6 hr in a clinkerization process, using a simulated incinerator and smelter . The major components of ordinary Portland cement, C3S, C2S, C3A, and C4AF, were all found in the clinkers . Of the three types of eco-cements, the eco-cement A paste was most similar to ordinary Portland cement in terms of composition and compressive strength development, while the eco-cement B paste showed early strength development . The differential thermal analysis species analyses indicated that the hydrates in the eco-cement pastes were mainly calcium hydroxide and CSH gels, like those found in ordinary Portland cement paste . Moreover, the degree of hydration, as determined by nuclear magnetic resonance, increased in all eco-cement pastes with an increasing curing age . The results indicate that it indeed is feasible to use sludge ash and ferrate to replace up to 20% of the mineral components of raw materials for cement. Riv Biol, 2004 Jan-Apr, 97(1), 67 - 78 Aquatic ecosystem as a bioreactor: water purification and some other functions; Ostroumov SA; A fundamental concept is proposed of aquatic ecosystem as a bioreactor that carries out the function of water purification in natural water bodies and streams . The ecosystem as a bioreactor has the following characteristic attributes: (1) it is a large-scale (large-volume) bioreactor; (2) it is a diversified (in terms of the number of taxa and the scope of functional activities) bioreactor; (3) it possesses a broad range of biocatalytic (chemical-transforming and degrading) capabilities . New experimental data on xenobiotics-induced inhibition of the functioning of the molluscs Unio tu- midus, U . pictorum, M . galloprovincialis and Limnaea stagnalis emphasize the potential ecological hazard from sublethal concentrations of pollutants (including those exemplified by synthetic surfactants and detergents). Arch Virol . 2005 Jan 13; {Epub ahead of print} Detection of enteric viruses and bacterial indicators in German environmental waters; Pusch D et al.; A German mining lake and the supplying surface waters, which are located downstream of a sewage plant, were examined regarding their microbiological and virological quality . Between October 2002 and September 2003, specific PCR methods were used to determine the occurrence of enteric viruses in 123 water specimens drawn at different sites downstream of the waste water treatment plant and in 9 samples from the sewage plant influent . Detection rates in sewage plant effluents and surface water samples depended on sampling sites and were: 29-76% for enterovirus (EntV), 24-42% (astrovirus, AstV), 15-53% (norovirus, NV), 3-24% (rotavirus, RoV), 5-20% (hepatitis A virus, HAV) and 20% (adenovirus, AdV) . AstV genome load of selected samples was between 3.7 x 10(3) to 1.2 x 10(8) genome equivalents per liter (gen.equ./l), depending on sampling location; NV average genome load ranged from 1.8 x 10(4) to 9.7 x 10(5) gen.equ./l . Cell culture methods showed that three out of 18 PCR positive samples contained infectious EntV . Even though microbiolical parameters such as Escherichia coli, enterococci and coliphages indicated acceptable microbiological water quality, the virological data of this study suggest the possibility that surface waters may be a source for enteric viral infections. Water Res, 2005 Jan-Feb, 39(2-3), 501 - 9 Epub 2004 Dec 20. Studies on the effect of humic acids and phenol on adsorption-ultrafiltration process performance; Mozia S et al.; Application of pressure-driven membrane processes, such as ultrafiltration (UF) and microfiltration (MF) for surface water treatment have become very popular during last decades . Membrane fouling by humic substances (HS) is one of the major limiting factors in these processes . In order to alleviate the unfavorable effects of the presence of HS in the feed on the process performance UF and MF are often combined with adsorption on powdered activated carbon (PAC) . The main goal of the present study was to evaluate the effect of humic acid (HA) on membrane fouling during UF . Moreover, the effect of PAC addition to the feed on UF process, especially on flux decline was determined . The applicability of the adsorption-ultrafiltration (PAC/UF) system to purification of water containing low (phenol) and high molecular (HA) was also investigated . Three different polymer UF membranes, prepared from polysulfone (PSF), cellulose acetate (CA) or polyacrylonitrile (PAN) were applied . It was found that the membranes prepared from PSF and CA are very susceptible to fouling caused by HA . The permeate flux decreased for ca . 50% during UF of HA solution through the PSF membrane and for ca . 45%-through the CA membrane . In the case of the PAN membrane, a negligible effect of HA on the flux was observed . On the basis of the FTIR spectra it was found that the drop in the permeate flux through these membranes may result from interactions between the negatively charged functional groups present on the membrane surface, such as carboxyl groups (CA) and sulfone groups (PSF) with HA, which results in coating of the membrane surface with HA . When PAC was added to the feed containing HA, the permeate flux through the CA and PAN membranes was maintained on a practically unchanged level . However, in case of the PSF membrane, a 50% drop in the permeate flux in comparison with the flux value, when process was conducted without PAC addition was observed . That was supposed to be due to attractive forces among hydrophobic PAC particles, HA molecules and PSF membrane surface . The performed studies showed that the application of PAC/UF system was very effective in the removal of organic substances having both, low and high molecular weights . The role of PAC suspended in a feed in the PAC/UF system is the adsorption of low molecular organic compounds, which cannot be removed by UF alone. Water Res, 2005 Jan-Feb, 39(2-3), 314 - 30 Epub 2004 Dec 08. Optimization of the extended terminal subfluidization wash (ETSW) filter backwashing procedure; Amburgey JE; The increased passage of particles and microorganisms through granular media filters immediately following backwashing is a common problem known to the water treatment community as filter "ripening" or maturation . While several strategies have been developed over the years to reduce the impact of this vulnerable period of the filtration cycle on finished water quality, this research involves a recently developed filter backwashing strategy called the extended terminal subfluidization wash (ETSW) . ETSW is a method of terminating the backwash cycle with a subfluidization wash for a period of time sufficient to pass one theoretical filter-volume of water upward through the filter . ETSW was shown to remove significantly greater quantities of backwash remnant particles thereby reducing the magnitude of filter ripening turbidity and particle count spikes . Optimum ETSW flow rates were determined for deep-bed anthracite and granular activated carbon filters herein by monitoring filter effluent turbidities and particle counts during the filter ripening period . Optimality of the coagulation process was also shown to influence the magnitude of filter ripening particle passage . ETSW was found to be equally effective for biological and conventional deep-bed anthracite filters. Water Res, 2005 Jan-Feb, 39(2-3), 305 - 13 Epub 2004 Dec 15. An improvement on the power law for the description of particle size distributions in potable water treatment; Ceronio AD et al.; In potable water treatment, the use of the power law to describe particle size distributions (PSDs) in particle counting practice is common . The power law is popular because it allows the reduction of numerous data bits to two meaningful parameters that completely describe the size distribution characteristics of a particle suspension . The model is however flawed . This paper presents the further development of an improved model (the variable-beta model) first proposed by Lawler (1997) . Both the power law model and variable-beta model are used to describe the PSDs of a large number of potable water treatment samples taken from full-scale plants and the resulting correlations are compared . The findings from the comparison of data reduction methodologies support the argument that the variable-beta model is fundamentally more correct than the power law model and consequently describes the PSDs better. Appl Environ Microbiol, 2005 Jan, 71(1), 131 - 9 Epidemiology of Cryptosporidium molnari in Spanish Gilthead Sea Bream (Sparus aurata L.) and European Sea Bass (Dicentrarchus labrax L.) Cultures: from Hatchery to Market Size; Sitja-Bobadilla A et al.; A long-term epidemiological study of Cryptosporidium molnari in aquacultured European sea bass (ESB) and gilthead sea bream (GSB) was performed in different types of facilities on the Atlantic, Cantabric, and Mediterranean coasts . Four types of studies were carried out . In study A, fish raised from juveniles to marketable size (ongrowing stage) were periodically sampled in three different types of cultures . Studies B and C focused on hatchery and nursery facilities . In study D, occasional samplings were performed during mortality or morbidity outbreaks . As a general trend, C . molnari was more prevalent in GSB than in ESB . Data on the distribution pattern of C . molnari in total sampled GSB (studies A, B, and D) had a variance higher than the mean (overdispersion) . In GSB (study A), the type of ongrowing system (sea cages, earth ponds, or indoor tanks) was found to have no significant effect . There was a significant relationship between the presence of the parasite and both fish weight and season . The highest infection values were recorded in spring . Prevalence and intensity had convex weight profiles, with a peak in 30- to 100-g fish . In study D, the prevalence of infection was higher in fish recently introduced in sea cages and in preongrowing systems . In studies B and C, fish were almost never infected before entering the postlarval and nursery facilities . The parasite seems to enter the host mainly through the water in production steps with less stringent water treatment . Recirculation systems and fish cannibalism could contribute to oocyst concentration and dispersion in aquaculture facilities. Int J Vitam Nutr Res, 2004 Sep, 74(5), 349 - 54 Melatonin improved the disturbances in hepatic prooxidant and antioxidant balance and hepatotoxicity induced by a high cholesterol diet in C57BL/6J mice; Balkan J et al.; We examined the effect of melatonin in prooxidant and antioxidant state in the liver of C57BL/6J mice fed on a high cholesterol (HC) diet . Mice were fed with normal mice chow containing 1.5% cholesterol and 0.5% cholic acid for 4 months without and with melatonin (10 mg/L in drinking water) treatment . HC diet was observed to increase malondialdehyde (MDA) and diene conjugate (DC) levels in the liver . This diet lowered glutathione (GSH), alpha-tocopherol, and total ascorbic acid levels as well as glutathione peroxidase (GSH-Px) and glutathione transferase (GST) activities in the liver, but hepatic superoxide dismutase (SOD) activity remained unchanged . Although melatonin treatment did not affect these parameters in mice fed a normal diet, it reduced hepatic MDA and DC levels in mice fed an HC diet . Hepatic alpha-tocopherol and ascorbic acid levels increased, but hepatic GSH levels remained unchanged in the melatonin-treated HC group as compared to the HC group . Melatonin treatment was found to increase liver GSH-Px and GST activities in mice fed an HC diet . However, SOD activity did not alter in the liver of hypercholesterolemic mice following melatonin treatment . In addition, the histopathological lesions observed in the cholesterol-plus-melatonin group were less severe than those seen in the cholesterol group . According to these observations, we can say that melatonin treatment has an ameliorating effect on the disturbances in prooxidant and antioxidant balance and histopathological lesions in the liver of mice following cholesterol feeding. Br Poult Sci, 2004 Oct, 45(5), 624 - 30 Comparative study of different surface decontaminants on chicken quality; Sinhamahapatra M et al.; (1) A comparative study on the effect of different surface decontaminants: hot water at 70 degrees C for one minute; 2% lactic acid for 30 s; 1200 p.p.m . acidified sodium chlorite (ASC) solution for 5 s and 50 p.p.m . chlorine solution for 5 min in the form of dips and sprays on the surface of dressed broilers for 0, 24 and 48 h of storage was conducted . (2) The variables studied were, total plate count (TPC), presumptive coliform count (PCC), pH and extract release volume (ERV) . All treatments reduced TPC and PCC . (3) Lactic acid dip and hot water dip were the most effective for reducing TPC (1.36 and 1.28 log/cm2, respectively) with no significant difference between them . (4) ASC and hot water in dip could diminish PCC (1.37 and 1.34 log/cm2, respectively) and did not vary significantly . (5) No treatment affected muscle pH, water holding capacity (WHC), ERV, appearance, smell, tenderness and overall acceptability of treated broilers significantly . (6) Hot water treatment is the cheapest, most convenient and simplest decontamination technique for hygienic and wholesome poultry production. Huan Jing Ke Xue, 2004 Sep, 25(5), 57 - 60 {Relationship between phosphorus and bacterial regrowth in drinking water}; Jiang DL et al.; Limitation of phosphorus on bacterial regrowth was studied in source water, water treatment process and a main distribution pipe of J waterwork in T city, by modified assimilable organic carbon (AOC) method and microbially available phosphorus (MAP) analysis . Based on the study, the result showed that: (1) Concentration of MAP was higher in source water and water treatment process, which was 5-38 microg/L (PO4(3-)-P) . However in water distribution system, concentration of MAP was lower, which was less than 5 microg/L (PO4(3-)-P) . It changed very little in distribution system . (2) Traditional treatment process can remove MAP efficiently 34.0%-83.7% of MAP can be removed in the process . (3) Generally in source water and water treatment process, there was no evident difference between AOC(potential), AOC(P) and AOC(native) . So AOC was the most important factor of bacterial growth . In the main distribution pipe, the concentration of AOC(potential) and AOC(P) were 2-8.7 times of the concentration of AOC(native) . So phosphorus limited bacterial regrowth. Environ Pollut, 2005 Apr, 134(3), 411 - 21 Performance of a constructed wetland treating intensive shrimp aquaculture wastewater under high hydraulic loading rate; Lin YF et al.; A water treatment unit, mainly consisting of free water surface (FWS) and subsurface flow (SF) constructed wetland cells, was integrated into a commercial-scale recirculating aquaculture system for intensive shrimp culture . This study investigated performance of the treatment wetlands for controlling water quality . The results showed that the FWS-SF cells effectively removed total suspended solids (55-66%), 5-day biochemical oxygen demand (37-54%), total ammonia (64-66%) and nitrite (83-94%) from the recirculating water under high hydraulic loading rates (1.57-1.95m/day) . This led to a water quality that was suitable for shrimp culture and effluent that always satisfied the discharge standards . The area ratios of wetlands to culture tank being demonstrated (0.43) and calculated (0.096) in this study were both significantly lower than the reported values . Accordingly, a constructed wetland was technically and economically feasible for managing water quality of an intensive aquaculture system. Lancet Infect Dis, 2005 Jan, 5(1), 42 - 52 Water, sanitation, and hygiene interventions to reduce diarrhoea in less developed countries: a systematic review and meta-analysis; Fewtrell L et al.; Many studies have reported the results of interventions to reduce illness through improvements in drinking water, sanitation facilities, and hygiene practices in less developed countries . There has, however, been no formal systematic review and meta-analysis comparing the evidence of the relative effectiveness of these interventions . We developed a comprehensive search strategy designed to identify all peer-reviewed articles, in any language, that presented water, sanitation, or hygiene interventions . We examined only those articles with specific measurement of diarrhoea morbidity as a health outcome in non-outbreak conditions . We screened the titles and, where necessary, the abstracts of 2120 publications . 46 studies were judged to contain relevant evidence and were reviewed in detail . Data were extracted from these studies and pooled by meta-analysis to provide summary estimates of the effectiveness of each type of intervention . All of the interventions studied were found to reduce significantly the risks of diarrhoeal illness . Most of the interventions had a similar degree of impact on diarrhoeal illness, with the relative risk estimates from the overall meta-analyses ranging between 0.63 and 0.75 . The results generally agree with those from previous reviews, but water quality interventions (point-of-use water treatment) were found to be more effective than previously thought, and multiple interventions (consisting of combined water, sanitation, and hygiene measures) were not more effective than interventions with a single focus . There is some evidence of publication bias in the findings from the hygiene and water treatment interventions. Poult Sci, 2004 Dec, 83(12), 2071 - 8 Efficacy of electrolyzed oxidizing water for the microbial safety and quality of eggs; Bialka KL et al.; During commercial processing, eggs are washed in an alkaline detergent and then rinsed with chlorine to reduce dirt, debris, and microorganism levels . The alkaline and acidic fractions of electrolyzed oxidizing (EO) water have the ability to fit into the 2-step commercial egg washing process easily if proven to be effective . Therefore, the efficacy of EO water to decontaminate Salmonella Enteritidis and Escherichia coli K12 on artificially inoculated shell eggs was investigated . For the in vitro study, eggs were soaked in alkaline EO water followed by soaking in acidic EO water at various temperatures and times . Treated eggs showed a reduction in population between > or = 0.6 to > or =2.6 log10 cfu/g of shell for S . Enteritidis and > or =0.9 and > or =2.6 log10 for E . coli K12 . Log10 reductions of 1.7 and 2.0 for S . Enteritidis and E . coli K12, respectively, were observed for typical commercial detergent-sanitizer treatments, whereas log10 reductions of > or =2.1 and > or =2.3 for S . Enteritidis and E . coli K12, respectively, were achieved using the EO water treatment . For the pilot-scale study, both fractions of EO water were compared with the detergent-sanitizer treatment using E . coli K12 . Log10 reductions of > or = 2.98 and > or = 2.91 were found using the EO water treatment and the detergent-sanitizer treatment, respectively. d, e, h, k. The effects of 2 treatments on egg quality were investigated . EO water and the detergent-sanitizer treatments did not significantly affect albumen height or eggshell strength; however, there were significant affects on cuticle presence . These results indicate that EO water has the potential to be used as a sanitizing agent for the egg washing process. J Environ Monit, 2005 Jan, 7(1), 43 - 51 Epub 2004 Nov 22. Polycyclic musks in the Ruhr catchment area-transport, discharges of waste water, and transformations of HHCB, AHTN and HHCB-lactone; Bester K; The polycyclic musk fragrance compounds HHCB (1,3,4,6,7,8-hexahydro-4,6,6,7,8,8-hexamethylcyclopenta-(g)-2-benzopyran; trade name, e.g . galaxolide{registered sign}) and AHTN (7-acetyl-1,1,3,4,4,6-hexamethyl-1,2,3,4-tetrahydronaphthalene, trade name, e.g . tonalide{registered sign}) and the transformation product of HHCB (HHCB-lactone) were analysed in surface water samples and sewage treatment plants (STP) effluents in the Ruhr megalopolis . The STPs were the dominant source for these pollutants . In the part of the river where the drinking water is extracted from the river, about 60 ng L(-1) HHCB, 10 ng L(-1) AHTN and 20-30 ng L(-1) HHCB-lactone were found as typical riverine concentrations, while none of the compounds were detected near the spring of the river . On the other hand sewage treatment plant effluents exhibited concentrations up to 600 ng L(-1) . The STP's effluent resulted in elevated concentrations in some parts of the river and in the lakes into which they discharge . As some of the plants emit HHCB-lactone with a significantly changed enantiomeric pattern, biotransformation of HHCB to HHCB-lactone occurs in some waste water treatment plants operating with activated sludge . In those parts of the river where no relevant discharges of waste water or fresh water takes place neither the concentration nor the pattern changes significantly . This holds true especially for the HHCB versus HHCB-lactone ratios which indicates degradation less than 15% of the HHCB inventory in the river Ruhr itself . In other rivers, such as the Rhine, higher levels of HHCB-lactone in comparison to HHCB were detected (ratio 1 {ratio} 1). Expert Rev Vaccines, 2004 Dec, 3(6), 669 - 71 Present and future control of cryptosporidiosis in humans and animals; Jenkins MC; Although water treatment processes to remove Cryptosporidium are improving and detection methods for identifying the parasite in water are becoming more sensitive, outbreaks of cryptosporidiosis continue in the human population . Animals, especially dairy calves, often become infected as C . parvum oocysts are present in high numbers, remain viable for long periods of time after excretion and no disinfectants, prophylactic or therapeutic reagents exist . Vaccination against C . parvum is being attempted in ruminants for the purpose of generating hyperimmune colostrum containing antibodies that may be effective in passive immunotherapy against cryptosporidiosis in the young . A number of recombinant C . parvum surface or internal antigens have been expressed by DNA-cloning technology . Immune colostrum specific for several recombinant C . parvum proteins have demonstrated efficacy in murine and ruminant models against cryptosporidiosis . The P23 and CP15 antigens appear to be the most promising candidates for vaccine development . Recent studies have demonstrated efficacy of the drug nitazoxanide against C . parvum infection in humans . In the near future, control of this parasitic disease in humans and animals will rely on a combination of passive immunotherapy and selective drug treatment. Bioresour Technol, 2005 Apr, 96(6), 665 - 71 Surimi wash water treatment for protein recovery: effect of chitosan-alginate complex concentration and treatment time on protein adsorption; Wibowo S et al.; Chitosan (Chi), a protein recovery agent for the treatment of aqueous food processing streams, appears to work by mechanical entrapment and electrostatic interaction of chitosan amino groups with anionic groups on proteins . Chitosan effectiveness for recovering soluble proteins from surimi wash water (SWW) is increased by complexation with alginate (Alg) and by adjusting complex concentration and treatment time . Flocculation at 20 degrees C with Chi-Alg at a 0.2 mixing ratio added as 20, 40, 100 and 150 mg/L SWW was aided by 5 min agitation at 130 rpm and then held at the same temperature for 30 min, 1 and 24 h . Turbidity measurements, protein determinations and qualitative FTIR analysis confirmed SWW protein adsorption which depended on Chi-Alg concentration and reaction time while turbidity reduction was affected by concentration only . No differences (p<0.05) in protein adsorption were found between 1 and 24 h . Using 100 mg Chi-Alg complex/L SWW for 1 h achieved 83% protein adsorption and 97% turbidity reduction. Water Sci Technol, 2004, 50(9), 183 - 8 Reuse of fresh water sludge in cement making; Pan R et al.; With the increasing demand for high quality water, a large quantity of chemical agent must be added in the water purification process, which in turn generates enormous amount of fresh water sludge . Of all the options for sludge disposal, sludge reuse has been considered most economical and environmentally sound . This study evaluated the possibility of incorporating fresh water sludge in the making of Portland cement through the sintering process . The goal was to search for the optimal condition to maximize the replacement of clay with the fresh water sludge . Characteristics of fresh water sludge were collected and analyzed . The analysis showed that water source and water treatment process dominate th characteristics, particularly the chemical composition of the fresh water sludge . The fresh water sludge was mixed with the cement clay in various percentages, from 0% to 100%, as raw material for cement-making . The effects of its addition on the sintering condition and the quality of cement were evaluated . The analysis of the clinkers showed that the addition of the fresh water sludge did not change the phase form and the f-CaO content of the cement . The compressive strength of the masonry increased with the increasing addition of fresh water sludge . All cement products made from various replacement ratios met the Chinese National Standard of first degree Portland cement. Water Sci Technol, 2004, 50(9), 99 - 105 Acidic and hydrogen peroxide treatment of polyaluminum chloride (PACL) sludge from water treatment; Kwon JH et al.; The water treatment sludge including coagulants cannot be easily removed by conventional dewatering methods . The possibility of hydrogen peroxide (H2O2) oxidation as a pretreatment to enhance the dewaterability of polyaluminum chloride (PACl) sludge from water works was investigated . H2O2 treatment alone was not effective but H2O2 treatment under acidic condition significantly reduced both the cake water content and specific resistance to filtration (SRF), indicating the enhancement of dewaterability and filterability . The filterability after acid/H2O2 treatment was comparable to polymer conditioning and even more dewatered cake than polymer conditioning was produced . By H202 combined with sulfuric acid (H2SO4), leached iron caused Fenton's reaction, which showed a potential to significantly reduce the amount of solids mass and to produce more compact cake with higher filterability. Ying Yong Sheng Tai Xue Bao, 2004 Aug, 15(8), 1487 - 90 {Research advance in polyphosphate-accumulating microorganisms in enhanced biological phosphorus removal process}; Zheng J et al.; This paper discussed the function of enhanced biological phosphorus removal (EBPR) in P pollution control, P containing wastewater treatment and P resources recovery, and summarized the metabolic characteristics, research progress and methodologies of polyphosphate-accumulating organisms (PAOs) . Although polyphosphate has been found in many organisms, only few of PAOs were isolated, cultured and identified . Culture medium formulation is the key to isolate PAOs and to study the microbial accumulation of polyphosphate, and the competition of glycogen-accumulating organisms (GAOs) with PAOs for carbon resources is one of the reasons of low EBPR efficiency . Modern scientific methods such as fluorescent in situ hybridization, confocal laser scanning microscope, microautoradiography, and in vivo NMR spectroscopy, provided powerful tools to analyze PAO species composition, spatial structure and functional properties under field conditions . The knowledge of PAO is valuable to enhance the P removal efficiency in water treatment plant, and to improve our understanding on P transformation and transferring in environment. Environ Sci Technol, 2004 Nov 15, 38(22), 6132 - 8 Particles in filter effluent: the roles of deposition and detachment; Kim J et al.; Particles in the effluent of granular media filters can be classified as influent particles that were never removed or as particles that detached after prior deposition . To determine the effects of particle size, filter media depth and filter run duration on the relative fraction of each class, laboratory experiments were performed using suspensions of four sizes of polystyrene particles (0.2, 1.2, 2.5, and 4.0 microm diameters) that were destabilized with 0.04 M calcium chloride and continuously supplied to filters after flocculation . To investigate particle attachment alone, three sizes (1.4, 4.0, and 9 microm) of fluorescent microspheres (FM) were periodically pulse injected immediately ahead of the filter media . Detachmentwas assessed as the difference between net removal (particle counts) and deposition (FM counts) . FM deposition followed theory, while results show that particle detachment was significant from an early phase of filtration (100 minutes) . The detached fraction of effluent particles increased with particle size (1 to 12 microm range) and filter depth . These model system results suggest that detachment plays a significant role in the origin of filter effluent particles in full-scale water treatment systems. Environ Sci Technol, 2004 Nov 15, 38(22), 6025 - 31 Oxidation of the cyanobacterial hepatotoxin microcystin-LR by chlorine dioxide: reaction kinetics, characterization, and toxicity of reaction products; Kull TP et al.; Cyanobacteria are known producers of cytotoxins, hepatotoxins, and neurotoxins . The main toxins are microcystins, cyclic heptapeptide hepatotoxins, produced by strains of several cyanobacterial genera frequently found in eutrophied freshwaters . Due to the acute and chronic toxicity of microcystins, successful removal of these toxins in drinking water treatment processes is of increasing concern . In the present work the kinetics of microcystin-LR (MC-LR) oxidation by chlorine dioxide (ClO2) was studied with UV-spectrometry and high performance liquid chromatography (HPLC) . Characterization of reaction products was performed with mass spectrometric (MS) analysis, while the toxicity of reaction products was tested with a protein phosphatase inhibition assay (PPIA) . The main reaction products formed, dihydroxy isomers of MC-LR as identified by MS, were nontoxic according to the PPIA . The overall rate constant k for the reaction between MC-LR and ClO2 at 293 K and pH 5.65 was modest, k = 1.24 M(-1) s(-1), suggesting that ClO2 is not a suitable oxidant for the degradation of microcystins in drinking water treatment processes. Prehospital Disaster Med, 2004 Jul-Sep, 19(3), 266 - 77 Remote site production of sterile purified water from available surface water; Taylor MA et al.; A water purification and sterilization device was tested for its functional capabilities . Challenge water consisting of potable water augmented with bacteria, endotoxin, virus, suspended solids, and dissociable ions (sodium chloride, lead or arsenic salts) was passed through the device . The product water quality attributes were analyzed . The device demonstrated reduction in bacteria of >7 logs, endotoxin was reduced by >4 logs, virus was reduced by >4 logs, and dissociable ions were reduced by >3 logs . The product water of the device met the limits for a range of chemical entities specified by the United States Pharmacopeia and Association for the Advancement of Medical Instrumentation . The product water met the quality attributes of Sterile Water for Injection, USP, Sterile Purified Water, USP, and the Water for Dialysis . The device provides a logistical advantage in reducing the weight of transport of packaged water by 83% and the cube by 67% . It operates manually by gravity and is disposable after a single use . The device provides an effective alternative to the transport and use of packaged sterile water in remote locations by production of sterile water at the point-of-need using available water . It also is capable of producing safe drinking water following the production of clinical waters . This device has been cleared by the US Food and Drug Administration for production of three liters Sterile Purified Water, USP from Environmental Protection Agency (EPA) grade drinking water. Plant Biol (Stuttg), 2004 Nov, 6(6), 715 - 20 The effect of fruit age on seed germinability of a heterocarpic species, Atriplex sagittata; Mandak B et al.; Atriplex sagittata is an annual heterocarpic plant that produces three different fruit types (termed A, B, and C) . To examine the consequence of heterocarpy on germinability patterns over long time periods, we compared seed germinability of different fruit types that had been stored for up to 8 years . While germinability of non-dormant type C fruits in distilled water was high (up to 100 %) in the first 2 years, it rapidly decreased over time . Dormant fruit types A and B showed increased germinability up to 7 years, though loss of germinability was lower for type B than for type A fruits . Eight-year-old fruits of all types had significantly lower germinability than younger fruits, probably due to loss of viability . Heterocarpy, therefore, ensures that emergence rates for seedlings of A . sagittata will be maintained over relatively long periods, even in years of strong disturbance when all adult plants may be destroyed . The experiment further showed that germinability of all fruit types in high concentrations of salt, as compared with water treatment, changed over the course of 8 years . Whilst dormant types (A and B) of A . sagittata show increased germinability with age of the seed in water treatment, they significantly lose germinability over time with salinity treatment . Type C fruit was not influenced by salt in the first year, but germinability rapidly decreased with time . It follows that the species is able to germinate under high salt concentration in the first year, but this advantage gradually disappears. Vet Parasitol, 2004 Dec 9, 126(1-2), 219 - 34 Drinking water treatment processes for removal of Cryptosporidium and Giardia; Betancourt WQ et al.; Major waterborne cryptosporidiosis and giardiasis outbreaks associated with contaminated drinking water have been linked to evidence of suboptimal treatment . Cryptosporidium parvum oocysts are particularly more resistant than Giardia lamblia cysts to removal and inactivation by conventional water treatment (coagulation, sedimentation, filtration and chlorine disinfection); therefore, extensive research has been focused on the optimization of treatment processes and application of new technologies to reduce concentrations of viable/infectious oocysts to a level that prevents disease . The majority of the data on the performance of treatment processes to remove cysts and oocysts from drinking water have been obtained from pilot-tests, with a few studies performed in full-scale conventional water treatment plants . These studies have demonstrated that protozoan cyst removal throughout all stages of the conventional treatment is largely influenced by the effectiveness of coagulation pretreatment, which along with clarification constitutes the first treatment barrier against protozoan breakthrough . Physical removal of waterborne Crytosporidium oocysts and Giardia cysts is ultimately achieved by properly functioning conventional filters, providing that effective pretreatment of the water is applied . Disinfection by chemical or physical methods is finally required to inactivate/remove the infectious life stages of these organisms . The effectiveness of conventional (chlorination) and alternative (chlorine dioxide, ozonation and ultra violet {UV} irradiation) disinfection procedures for inactivation of Cryptosporidium has been the focus of much research due to the recalcitrant nature of waterborne oocysts to disinfectants . This paper provides technical information on conventional and alternative drinking water treatment technologies for removal and inactivation of the protozoan parasites Cryptosporidium and Giardia. Water Sci Technol, 2004, 50(8), 57 - 63 Monitoring of COD as an organic indicator in waste water and treated effluent by fluorescence excitation-emission (FEEM) matrix characterization; Lee S et al.; The fluorescence excitation-emission matrices (FEEM) of domestic waste water, treated effluent of a waste water treatment plant and receiving river water were analyzed to select wavelengths for the monitoring of organic contents as COD . Excitation/emission wavelengths of 220/350 nm and 270/350 nm for protein-like fluorescence and 240/450 nm and 340/450 nm for humic-like fluorescence were suggested as fluorescence peak emitting wavelength pairs, respectively . Without any pre-treatment, the protein-like fluorescence peaks showed better correlation between COD values and fluorescence intensities than the humic-like fluorescence peaks . No enhanced correlation was observed by removing the suspended solids from the samples using filtration . However, statistical multiple regression methods, using the fluorescence intensities from each peak and the light scattering intensity at 633 nm as variables, resulted in an enhanced correlation, with r2 > 0.9 for the measured and predicted COD values. Environ Toxicol Chem, 2004 Nov, 23(11), 2709 - 18 Using artificial streams to assess the effects of metal-mining effluent on the life cycle of the freshwater midge (Chironomus tentans) in situ; Hruska KA et al.; In 2002, we developed an in situ life-cycle bioassay with Chironomus tentans in artificial streams to evaluate the effects of a complex metal mine effluent under ambient environmental conditions . The bioassay was tested in the field using effluent from the Copper Cliff Waste Water Treatment Plant at INCO (Sudbury, ON, Canada) . Chironomus tentans were exposed throughout the life cycle to 45% Copper Cliff effluent, which is the average effluent concentration measured in Junction Creek (ON, Canada), the natural receiving environment . Chironomus tentans in the effluent treatment exhibited reduced survival (p = 0.001), reduced total emergence (p = 0.001), increased time-to-emergence (p = 0.001), and reduced hatching success (p = 0.001) relative to animals in the reference water treatment. c, l, c, g, i, k. Chironomus tentans in the effluent treatment were not significantly different from the reference in terms of growth, sex ratio, number of egg cases/female, and number of eggs/egg case . This research showed how a life-cycle bioassay could be used in situ to assess metal mine effluent effects on a benthic invertebrate. Water Res, 2004 Dec, 38(20), 4511 - 23 Identification and understanding of fouling in low-pressure membrane (MF/UF) filtration by natural organic matter (NOM); Lee N et al.; An understanding of natural organic matter (NOM) as a membrane foulant and the behavior of NOM components in low-pressure membrane fouling are needed to provide a basis for appropriate selection and operation of membrane technology for drinking water treatment . Fouling by NOM was investigated by employing several innovative chemical and morphological analyses . Source (feed) waters with a high hydrophilic (HPI) fraction content of NOM resulted in significant flux decline . Macromolecules of a relatively hydrophilic character (e.g . polysaccharides) were effectively rejected by low-pressure membranes, suggesting that macromolecular compounds and/or colloidal organic matter in the hydrophilic NOM fraction may be a problematic foulant of low-pressure membranes . Moreover, the significant organic fouling that is contributed by polysaccharides and/or proteins in macromolecular and/or colloidal forms depends on molecular shape (structure) as well as size (i.e . molecular weight) . More significant flux decline was observed in microfiltration (MF) compared to ultrafiltration (UF) membrane filtration . MF membrane fouling may be caused by pore blockage associated with large (macromolecular) hydrophilic molecules and/or organic colloids . In the case of UF membranes, the flux decline may be caused by sequential or simultaneous processes of surface (gel layer) coverage during filtration . Morphological analyses support the notion that membrane roughness may be considered as a more important factor in membrane fouling by controlling interaction between molecules and the membrane surface, compared to the hydrophobic/hydrophilic character of membranes . Membrane fouling mechanisms are not only a function of membrane type (MF versus UF) but also depend on source (feed) water characteristics. Water Sci Technol, 2004, 50(7), 265 - 71 Benchmarking of municipal waste water treatment plants (an Austrian project); Lindtner S et al.; An Austrian research project focused on the development of process indicators for treatment plants with different process and operation modes . The whole treatment scheme was subdivided into four processes, i.e . mechanical pretreatment (Process 1), mechanical-biological waste water treatment (Process 2), sludge thickening and stabilisation (Process 3) and further sludge treatment and disposal (Process 4) . In order to get comparable process indicators it was necessary to subdivide the sample of 76 individual treatment plants all over Austria into five groups according to their mean organic load (COD) in the influent . The specific total yearly costs, the yearly operating costs and the yearly capital costs of the four processes have been related to the yearly average of the measured organic load expressed in COD (110 g COD/pe/d) . The specific investment costs for the whole treatment plant and for Process 2 have been related to a calculated standard design capacity of the mechanical-biological part of the treatment plant expressed in COD . The capital costs of processes 1, 3 and 4 have been related to the design capacity of the treatment plant . For each group (related to the size of the plant) a benchmark band has been defined for the total yearly costs, the total yearly operational costs and the total yearly capital costs . For the operational costs of the Processes 1 to 4 one benchmark ({see symbol in text} per pe/year) has been defined for each group . In addition a theoretical cost reduction potential has been calculated . The cost efficiency in regard to water protection and some special sub-processes such as aeration and sludge dewatering has been analysed. Water Sci Technol, 2004, 50(7), 229 - 36 A new side stream process for easily degradable industrial waste waters to avoid sludge bulking; Wandl G et al.; A new treatment scheme for the treatment of easily biodegradable industrial waste waters has been developed . The side stream treatment of dairy waste water with the excess sludge from the domestic treatment line of the regional treatment plant Bad Voslau has been operated successfully for a period of three years during which the industrial load stemming from the dairy increased from 800 kg COD/d to 2,500 kg COD/d with peak loads up to 5,000 kg/d . Despite of the increased load to the treatment plant the total aeration tank volume had not been increased . This treatment is performed in an existing aeration tank of the WWTP (V = 1,800 m3) which is now used as contact tank for the combined aeration of dairy waste water and excess sludge from the domestic treatment line (volume aeration tank = 15,000 m3) . In this tank the easily degradable substrate from the industrial waste is mainly adsorbed to the biological sludge and after a mechanical dewatering transferred to the anaerobic digester where it yields in an increased gas production . The filtrate of the dewatering process is completely free from biodegradable material and can without danger of bulking be fed to the aeration tank of the domestic treatment line . The new process has proven to be extremely flexible since already now daily peak loads exceeding the design load by more then 60% could be treated in the plant without any problems . Compared to other alternatives for the dairy waste water treatment that were investigated during this study, the new side stream process is very advantageous . No other pre-treatment process for industrial waste water could have been operated under comparable loading conditions without severe operating problems. Environ Sci Technol, 2004 Oct 15, 38(20), 5476 - 83 Degradation of endocrine disrupting chemicals bisphenol A, ethinyl estradiol, and estradiol during UV photolysis and advanced oxidation processes; Rosenfeldt EJ et al.; The degradation of three endocrine disrupting chemicals (EDCs), bisphenol A, ethinyl estradiol, and estradiol, was investigated via ultraviolet (UV) radiation photolysis and the UV/hydrogen peroxide advanced oxidation process (AOP) . These EDCs have been detected at low levels in wastewaters and surface waters in both the United States and European countries, can cause adverse effects on humans and wildlife via interactions with the endocrine system, and thus must be treated before entering the public drinking water supply . Because many EDCs can only be partially removed with conventional water treatment systems, there is a need to evaluate alternative treatment processes . For each EDC tested, direct UV photolysis quantum yields were derived for use with both monochromatic low-pressure (LP) UV lamps and polychromatic medium-pressure (MP) UV lamps and second-order hydroxyl radical rate constants were developed . These parameters were utilized to successfully model UV treatment of the EDCs in laboratory and natural waters . The polychromatic MP UV radiation source was more effective for direct photolysis degradation as compared to conventional LP UV lamps emitting monochromatic UV 254 nm radiation . However, in all cases the EDCs were more effectively degraded utilizing UV/H2O2 advanced oxidation as compared to direct UV photolysis treatment. Environ Sci Technol, 2004 Oct 15, 38(20), 5365 - 72 Accumulation of arsenic in drinking water distribution systems; Lytle DA et al.; The tendency for iron solid surfaces to adsorb arsenic is well-known and has become the basis for several drinking water treatment approaches that remove arsenic . It is reasonable to assume that iron-based solids, such as corrosion deposits present in drinking water distribution systems, have similar adsorptive properties and could therefore concentrate arsenic and potentially re-release it into the distribution system . The arsenic composition of solids collected from drinking water distribution systems (pipe sections and hydrant flush solids), where the waters had measurable amounts of arsenic in their treated water, were determined . The elemental composition and mineralogy of 67 solid samples collected from 15 drinking water utilities located in Ohio (7), Michigan (7), and Indiana (1) were also determined . The arsenic content of these solids ranged from 10 to 13 650 microg of As/g of solid (as high as 1.37 wt %), and the major element of most solids was iron . Significant amounts of arsenic were even found in solids from systems that were exposed to relatively low concentrations of arsenic (<10 microg/L) in the water. Anal Chem, 2004 Nov 15, 76(22), 6548 - 54 Determination of polar drug residues in sewage and surface water applying liquid chromatography-tandem mass spectrometry; Zuehlke S et al.; A simple and rapid method is presented for the trace-level analysis of 10 polar pharmaceutical residues in various types of water samples from the aquatic environment . Using this method, the pharmaceuticals and several drug metabolites can be analyzed in drinking and surface waters and in wastewater (treated and untreated sewage) at concentrations down to 0.01 microg/L . Samples are prepared by a simple in situ derivatization enabling the preconcentration of very polar metabolites by automated solid-phase extraction . The analytes were separated by liquid chromatography with tandem mass spectrometric detection and quantified by comparison with an internal standard . Limits of quantification were between 0.01 and 0.02 microg/L for three phenazone-type pharmaceuticals, six of their metabolites, and the antiepileptic drug carbamazepine . Except for dimethylaminophenazone, recoveries for all analytes were between 87 and 117% for raw and purified sewage, groundwater, and surface and drinking water . Investigations of some environmental samples revealed that sewage and surface water treatment causes a slight reduction of the concentrations of some analytes whereas other compounds were persistent during water treatment . Thus, some compounds were detected at the low-microgram per liter level in sewage effluents of wastewater treatment plants in Berlin (Germany) and were also found at high-nanogram per liter concentrations in Berlin surface water samples. J Toxicol Clin Toxicol, 2004, 42(6), 897 - 900 Rapid cyanide detection using the Cyantesmo kit; Rella J et al.; BACKGROUND: Sources of cyanide exposure are many, including combustion of plastic and vinyl, such as in a house fire, laboratory or industrial exposures including exposure in the electroplating industry both of printed circuit boards and in jewelry work . Rapid and definitive diagnosis of cyanide poisoning is unavailable in the emergency department setting . It is desirable to make a definitive diagnosis in order to prevent potential complications of empiric treatment of presumptive cyanide poisoning from the cyanide antidote kit currently approved by the US Food and Drug Administration (FDA) . We investigated a technique to detect cyanide currently utilized by water treatment facilities to determine if it can be applied to rapidly detect concentrations of cyanide in the clinically important range . METHODS: Varying standardized dilutions of KCN ranging from 0.25 microg/mL to 30 microg/mL were acidified with a drop of sulphuric acid in a closed system under a ventilation hood . Cyantesmo test strips were placed into the test tubes above the fluid level where liberated HCN gas interacted with the test strip to effect a color change . Color changes were compared to negative controls and to each other . RESULTS: The test strips demonstrated an incrementally increasing deep blue color change over a progressively longer portion of the test strip in less than 5 minutes for each concentration of KCN including 1, 3, 10, and 30 microg/mL . The concentrations of 0.25, 0.5, and 0.75 required more than 2 hours to begin demonstration of any color change . CONCLUSION: The Cyantesmo test strips accurately and rapidly detected, in a semi-quantifiable manner, concentrations of CN greater than 1 microg/mL contained in each test sample . Future work to validate this test in blood and in clinical specimens is planned. J Environ Sci Health A Tox Hazard Subst Environ Eng, 2004, 39(11-12), 2835 - 53 Investigation of the formation of chlorination by-products in water rich in bromide and organic matter content; Nikolaou AD; Bench-scale chlorination experiments with river water rich in bromide and organic matter content were performed in order to investigate the behavior and speciation of the chlorination by-products, especially the brominated ones, which are considered more harmful to human health than their chlorinated analogues . The analysis of the compounds was performed by means of gas chromatography . Statistical treatment of the results with Multifactor Analysis of Variance technique revealed the trends of each compound as function of pH, chlorine dose, reaction time and temperature . Brominated species of chlorination by-products predominated, due to the presence of bromide in the river water leading to preferable bromination than chlorination of the organic matter . Bromide incorporation factors were calculated for trihalomethanes and haloacetic acids, the major categories of compounds formed . While bromide incorporation factors decreased with increasing chlorine dose, the opposite was true for low range of chlorine dose, a fact that needs to be considered during treatment of waters with similar properties . Bromide incorporation factors decreased with increasing pH, especially for haloacetic acids . While the organic matter content can be sufficiently removed during water treatment, bromide ion still remains in the treated water . The results of the present study indicate that chlorination conditions should be optimized in order to minimize the incorporation of bromide into the chlorination by-products formed, which would increase their toxic effects on the water consumers. Environ Pollut, 2005 Jan, 133(2), 183 - 98 Environmental applications for biosurfactants; Mulligan CN; Biosurfactants are surfactants that are produced extracellularly or as part of the cell membrane by bacteria, yeasts and fungi . Examples include Pseudomonas aeruginosa which produces rhamnolipids, Candida (formerly Torulopsis) bombicola, one of the few yeasts to produce biosurfactants, which produces high yields of sophorolipids from vegetable oils and sugars and Bacillus subtilis which produces a lipopeptide called surfactin . This review includes environmental applications of these biosurfactants for soil and water treatment . Biosurfactant applications in the environmental industries are promising due to their biodegradability, low toxicity and effectiveness in enhancing biodegradation and solubilization of low solubility compounds . However, more information is needed to be able to predict and model their behaviour . Full scale tests will be required . The role of biosurfactants in natural attenuation processes has not been determined . Very little information is available concerning the influence of soil components on the remediation process with biosurfactants . As most of the research until now has been performed with rhamnolipids, other biosurfactants need to be investigated as they may have more promising properties. Environ Technol, 2004 Sep, 25(9), 1067 - 76 Equilibrium, kinetic and mass transfer studies and column operations for the removal of arsenic(III) from aqueous solutions using acid treated spent bleaching earth; Mahramanlioglu M et al.; In the present study, a new adsorbent was produced from spent bleaching earth by H2SO4 impregnation method . The sorption of arsenic(III) by acid treated spent bleaching earth was studied to examine the possibility of utilizing this material in water treatment systems . The effect of time, pH, initial concentration, temperature on the adsorption of arsenic(III) was studied . Maximum adsorption was found to occur at pH 9.0 . The adsorption process followed the first order Lagergren equation . Mass transfer coefficients and rate constants of intraparticle diffusion were calculated . The experimental data points were fitted to the Langmuir equation in order to calculate the adsorption capacity (Q0) of the adsorbent and the value of Q0 was found to be 0.46 mmol g(-1) . In order to understand the adsorption mechanism, Dubinin-Radushkevich (DR) isotherm was used . The magnitude of E calculated from DR equation was found to be 5.12 kJ mol(-1) . The heat of adsorption (deltaH0 = -30367 J mol(-1)) implied that the adsorption was physical exothermic adsorption . The column studies were also carried out to simulate water treatment processes . The capacity values obtained in column studies were found to be greater than the capacity values obtained in batch studies . This result was explained by the difference between batch system and column system . The factors that affect the capacity values of column and batch systems were explained . The effect of other anions on the adsorption of arsenic(III) in the presence of NO3-, SO4(2-), Cl-, Br- was studied . The presence of these anions did not affect the adsorption of arsenic(III) significantly. Environ Technol, 2004 Sep, 25(9), 1051 - 7 Wastewater sludge convective drying: influence of sludge origin; Leonard A et al.; This paper deals with thermal drying of wastewater sludges, whose management will become crucial in the forthcoming years . Sludges collected after mechanical dewatering in 5 different WWTPs are submitted to the same convective drying treatment in order to try finding some relations between the drying behaviours, the type of effluent and wastewater treatments . Results show dearly sludge drying remains a particularly complex operation because sludges may exhibit very different behaviours, both from kinetic and texture points of view . Initial moisture content and global composition are not sufficient to explain the different observed behaviours . It is too early to claim one or another type of water treatment has an influence on the drying behaviour . However, the drying rates can be classified in the inverse order of the organic content . Moreover for sludges at the same siccities, the harder the material (rheological properties), the higher the drying rate . Final textural properties can be related to the rheological properties and the internal diffusion limitations lowering the drying intensity. Sci Prog, 2003, 86(Pt 4), 313 - 32 UV radiation-induced enterobacterial responses, other processes that influence UV tolerance and likely environmental significance; Rowbury RJ; The ability of enterobacteria to become UV-tolerant is important because such tolerance may enable organisms to resist irradiation in the environment, in water treatment, in shell-fish, in stages of food processing, and at locations in the domestic, commercial and hospital environment The mechanism for regulation of tolerance induction and SOS response induction has been studied for many years, and is well understood, except for the early stages of induction . Such early stages, namely sensing of the stimulus (UV irradiation) and the way in which such sensing leads to signal production, have until now been poorly understood . The claim has been made that DNA is the sensor and that either damage to DNA or production of SS regions in DNA (following interaction of UV with DNA) triggers the signal that sets in train RecA activation and other stages of tolerance induction . This claimed induction mechanism is a "classical" one in the sense that it involves intracellular sensing (by DNA) of the stressing stimulus (UV), and production of an intracellular signalling molecule . It is not, however, firmly established as the mechanism for initiation of UV tolerance induction and SOS response induction . The results reviewed here give firm evidence for a different and unique mechanism for sensing of UV and production of the signal . These results establish without doubt that, for UV tolerance induction, the UV sensor is an extracellular protein, which is a UV tolerance-specific extracellular sensing component (ESC) . This component is formed by unstressed cells and on interacting with the stimulus (UV) in the medium, is converted to the tolerance induction signalling molecule, which is a UV tolerance-specific extracellular induction component (EIC) . It is this extracellular signal which interacts with the sensitive organisms and triggers tolerance induction . This pair of extracellular components (ECs) may offer the only means of switching-on such tolerance induction; certainly they offer the only known way for early warning to be given of impending UV challenge . Thus, the EIC can diffuse from a region of UV stress to a stress-free region and there warn organisms of impending stress and prepare them to resist it. d, h, k, k. As indicated here, UV irradiation not only induces UV tolerance, but also switches-on acid tolerance, alkali tolerance and thermotolerance responses . The fact that all three responses involve ESC/EIC pairs strongly supports the view that functioning of such EC pairs form the major, if not the only, means for UV tolerance induction . The UV tolerance-specific ESC can detect other stresses and becomes activated, leading to cross-tolerance responses . Of particular interest, this ESC acts as a biological thermometer, detecting increases in temperature, such increases leading to gradually increasing formation of the EIC and, accordingly, gradual increases in UV tolerance . This UV tolerance-specific ESC can also detect other stresses e.g . acting as a pH sensor . In all cases, on activation, the EIC formed (from this specific ESC) only induces UV tolerance . It is proposed that the interaction of EICs with stress-sensitive organisms should be examined, and it is suggested that such EICs may, directly or indirectly, interact with and activate the same stress response regulators as are used to detect internal stressors and which, on activation, also trigger the switching-on of stress responses . For example, EICs either a in a protonated or oxidised state (formed by activation of ESCs by H+ or H2O2) or b produced by irradiation, may lead to protonation or oxidation or other forms of activation of the appropriate regulator (e.g . Fur or OxyR or RecA etc), leading to response induction. Environ Sci Technol, 2004 Oct 1, 38(19), 5187 - 95 Enhanced bromate control during ozonation: the chlorine-ammonia process; Buffle MO et al.; Potentially carcinogenic bromate forms during the ozonation of bromide-containing waters . Some water treatment facilities have had to use ammonia addition and pH depression to minimize bromate formation, but these processes may prove to be insufficient to comply with upcoming regulations . The chlorine-ammonia process (Cl2-NH3), consisting of prechlorination followed by ammonia addition priorto ozonation is shown to cause a 4-fold decrease in bromate formed when compared to the ammonia-only process . Experiments revealed three key mechanisms: (i) oxidation by HOCl of Br- to HOBr and its subsequent masking by NH3 as NH2Br; (ii) decrease of HO- exposure through halogenation of Dissolved Natural Organic Matter (DNOM) by HOCI and scavenging of HO by NH2Cl; and (iii) DNOM acting as a bromine sink after oxidation of Br- to HOBr . At an ozone exposure of 6 mg/L x min and pH 8, conventional ozonation of Lake Zurich water spiked with 560 microg/L Br- formed 35 microg/L BrO3-, whereas the application of the Cl2-NH3 process resulted in 5 microg/L BrO3- . Additional pH depression to pH 6 further decreased bromate formation by a factor of 4 . Trihalomethanes (THM) and cyanogen chloride (CNCl), that mayform during prechlorination and monochloramination, respectively, were well below regulatory limits . The chlorine-ammonia process holds strong promise for water treatment facilities struggling with a bromate formation problem during ozonation. Environ Sci Technol, 2004 Oct 1, 38(19), 5164 - 9 Laboratory assessment of the mobility of nanomaterials in porous media; Lecoanet HF et al.; The production of significant quantities of engineered nanomaterials will inevitably result in the introduction of these materials to the environment . Mobility in a well-defined porous medium was evaluated for eight particulate products of nanochemistry to assess their potential for migration in porous media such as groundwater aquifers and water treatment plant filters . Contrary to the assertion that nanomaterials present monolithic environmental risks, here we show that these nanomaterials exhibit widely differing transport behaviors . Fullerene-based nanomaterials that had been functionalized to facilitate dispersal in water displayed the highest mobilities, with a calculated potential to migrate approximately 10 m in unfractured sand aquifers . Colloidal aggregates of C60, which have been the focus of recent toxicity studies, were among the least mobile of the nanomaterials evaluated. Environ Sci Technol, 2004 Oct 1, 38(19), 5157 - 63 Chloride effect on TNT degradation by zerovalent iron or zinc during water treatment; Hernandez R et al.; Addition of corrosion promoters, such as sodium and potassium chloride, accelerated TNT degradation during water treatment using zerovalent zinc and iron . It was theorized that corrosion promoters could be used to accelerate electron generation from metallic species, create new reactive sites on the surface of metals during contaminated water treatment, and minimize passivating effects . The surface area normalized pseudo-first-order rate constant for the reaction of zerovalent zinc with TNT in the absence of KCl was 1.364 L x m(-2) x h(-1) . In the presence of 0.3 mM and 3 mM KCI, the rate constant increased to 10.5 L x m(-2) x h(-1) and 51.0 L x m(-2) x h(-1), respectively . For the reaction with zerovalent iron and TNT, the rate constant increased from 6.5 (L/m2 x h) in the absence of KCl to 37 L x m(-2) x h(-1) using 3 mM KCl . The results demonstrate that chloride based corrosion promoters enhance the rate of TNT degradation . The in-situ breakage of the oxide layer using corrosion promoters was applied as a treatment to maintain the long-term activity of the metallic species . Zinc maintained a high reactivity toward TNT, and the reactivity of iron increased after 5 treatment cycles using 3 mM KCI . Zinc and iron scanning electron micrographs indicate that TNT degradation rate enhancement is caused by the pitting corrosion mechanism. Chemosphere, 2004 Dec, 57(9), 1115 - 22 Determining the effectiveness of conventional and alternative coagulants through effective characterization schemes; Sinha S et al.; Polymeric forms of metal coagulants in water treatment have become increasingly used due to their wider availability and reduction in cost . These specialized coagulant forms and products are claimed by manufacturers to be superior to conventional coagulants in particulate and/or organic removal with inherent advantages of lower alkalinity consumption and lesser sludge production . However, due to their proprietary nature, little is known about their chemical composition . To determine and understand the effectiveness of these alternative coagulants, a comprehensive study was undertaken to characterize metal coagulants, and to comparatively evaluate them on a well-characterized source water . The objective of this study was to provide a scheme for utilities that could be employed as a screening process and a method of selecting an appropriate coagulant based on raw water characteristics and insight into the coagulatability of the source water . Characterizations of coagulants included: (i) active metal content, (ii) anion content, (iii) acidity, (iv) alkalinity consumption, (v) charge reversal by colloidal titration, and (vi) molecular weight determination . A total of five poly-aluminum chlorides (PACl), along with a conventional coagulant (aluminum sulfate or alum) were evaluated . Results show that through the characterization scheme, an effective coagulant (conventional versus alternative) and coagulant type (among various PACl) can be chosen before undertaking time-consuming bench or pilot-scale evaluation. Res Microbiol, 2004 Nov, 155(9), 726 - 30 Survival and injury of Arcobacter after artificial inoculation into drinking water; Moreno Y et al.; The aim of this work was to assess the effect of chlorine water treatment on Arcobacter butzleri and to study the survival strategies of this organism in chlorinated and non-chlorinated drinking water . A . butzleri NCTC 12481 was inoculated into chlorinated and non-chlorinated water and samples were removed aseptically, immediately and periodically during the next 2 days (for chlorinated drinking water) or 35 days (for non-chlorinated drinking water) . The membrane integrity (Live/Dead BacLight kit), 16S rRNA (FISH technique), DNA content (23S rRNA PCR-RFLPs) and culturability changes in A . butzleri cells were analyzed . Culturability of the cells was lost at 5 min in chlorinated drinking water . At that time the cells showed membrane damage, although fluorescent intensity of 16S rRNA hybridization was constant throughout the chlorine treatment . After 48 h the amplicon specific for the 23S rRNA gene was weakly detected . In non-chlorinated drinking water cells lost their culturability after 16 days but the other factors measured indicated that Arcobacter remained viable throughout the experiment. MMWR Surveill Summ, 2004 Oct 22, 53(8), 1 - 22 Surveillance for waterborne-disease outbreaks associated with recreational water--United States, 2001-2002; Yoder JS et al.; PROBLEM/CONDITION: Since 1971, CDC, the U.S . Environmental Protection Agency, and the Council of State and Territorial Epidemiologists have maintained a collaborative surveillance system for collecting and periodically reporting data related to occurrences and causes of waterborne-disease outbreaks (WBDOs) related to drinking water; tabulation of recreational water-associated outbreaks was added to the surveillance system in 1978 . This surveillance system is the primary source of data concerning the scope and effects of waterborne disease outbreaks on persons in the United States . REPORTING PERIOD COVERED: This summary includes data on WBDOs associated with recreational water that occurred during January 2001-December 2002 and on a previously unreported outbreak that occurred during 1998 . DESCRIPTION OF SYSTEM: Public health departments in the states, territories, localities, and the Freely Associated States are primarily responsible for detecting and investigating WBDOs and voluntarily reporting them to CDC on a standard form . The surveillance system includes data for outbreaks associated with both drinking water and recreational water; only outbreaks associated with recreational water are reported in this summary . RESULTS: During 2001-2002, a total of 65 WBDOs associated with recreational water were reported by 23 states . These 65 outbreaks caused illness among an estimated 2,536 persons; 61 persons were hospitalized, eight of whom died . This is the largest number of recreational water-associated outbreaks to occur since reporting began in 1978; the number of recreational water-associated outbreaks has increased significantly during this period (p<0.01) . Of these 65 outbreaks, 30 (46.2%) involved gastroenteritis . The etiologic agent was identified in 23 (76.7%) of these 30 outbreaks; 18 (60.0%) of the 30 were associated with swimming or wading pools . Eight (12.3%) of the 65 recreational water-associated disease outbreaks were attributed to single cases of primary amebic meningoencephalitis caused by Naegleria fowleri; all eight cases were fatal and were associated with swimming in a lake (n = seven; 87.5%) or river (n = one; 12.5%) . Of the 65 outbreaks, 21 (32.3%) involved dermatitis; 20 (95.2%) of these 21 outbreaks were associated with spas or pools . In addition, one outbreak of Pontiac fever associated with a spa was reported to CDC . Four (6.1%) of the 65 outbreaks involved acute respiratory illness associated with chemical exposure at pools . INTERPRETATION: The 30 outbreaks involving gastroenteritis comprised the largest proportion of recreational water-associated outbreaks during this reporting period . These outbreaks were associated most frequently with Cryptosporidium (50.0%) in treated water venues and with toxigenic Escherichia coli (25.0%) and norovirus (25.0%) in freshwater venues . The increase in the number of outbreaks since 1993 could reflect improved surveillance and reporting at the local and state level, a true increase in the number of WBDOs, or a combination of these factors . PUBLIC HEALTH ACTION: CDC uses surveillance data to identify the etiologic agents, types of aquatics venues, water-treatment systems, and deficiencies associated with outbreaks and to evaluate the adequacy of efforts (e.g., regulations and public awareness activities) for providing safe recreational water . Surveillance data are also used to establish public health prevention priorities, which might lead to improved water-quality regulations at the local, state, and federal levels. Water Sci Technol, 2004, 50(5), 369 - 72 Re-evaluation and re-construction of water purification system using soil . II . Removal of pollutants from infiltrating water; Hamasaki T et al.; Presented in this paper are the results of a series of column experiments and a pilot scale test conducted to develop the treatment system of freshwater and wastewater by their percolation through soil and the other materials at the rate of a few metres per day . Materials that had high ability to sorb fulvic acid (FA hereafter) and phosphate ion were selected based on the results of the batch sorption tests and were processed into beads before subjecting them to the column test . The results of the column experiment suggested that the reagents added to increase the strength of the beads reduced the sorption of FA, thus causing the early breakthrough of the FA injected into the column . Less effect from the bead processing was observed for the removal of phosphate ion . Pilot scale test showed that the removal of particulate fraction of phosphorus differed among the materials used . The bead processing technique that can ensure the high water permeability while maintaining the sorption capacity of the material was required for further development of the treatment system. Water Sci Technol, 2004, 50(5), 363 - 7 Re-evaluation and reconstruction of water purification system using soil . I . Assessment of soil as a sorbent of humic substances and phosphate ion; Fujikawa Y et al.; The purpose of our study is to develop a treatment procedure for humic substances (HS hereafter) and phosphate ion in wastewater and environmental water by percolation of the water through a constructed soil layer at the hydraulic loading of a few metres per day . In the present work, batch sorption tests were conducted for more than 80 samples of soil, sludge, mineral and organic materials in order to find good sorbents for fulvic acid (FA hereafter) and phosphate ion . The results showed that the sorption of FA was high for some charcoal, and apatite and goethite minerals . Comparatively high sorption of FA was found for some Andosols and volcanic ash soil . Significant sorption of phosphate ion, on the other hand, was found for various types of soil, sludge from water treatment plants and some waste materials . The linear isotherm was obtained for the sorption of FA to a charcoal, apatite and goethite minerals, and Andosols. Water Sci Technol, 2004, 50(5), 243 - 51 Integrated systems analysis of persistent polar pollutants in the water cycle; van der Voet E et al.; Persistent polar pollutants (P3) are difficult to degrade in standard waste water treatment plants . As a result, they end up in the effluent and are emitted to the surface water . In some areas, this problem is aggravated through "closed loop recycling", causing concentrations of P3 in surface water to build up over time . This could cause violation of (future) EU regulations . In the P-THREE project, various alternative waste water treatment techniques are investigated regarding their effectiveness in eliminating these substances, especially membrane bioreactor treatment and advanced oxidation processes, MBR and AOP . The integrated systems analysis which is the subject of this paper assesses these techniques in a broader systems context: (1) the life-cycle of the P3, (2) the life cycle of the WWTPs, and (3) the WWTP life cycle costs. Water Sci Technol, 2004, 50(5), 165 - 71 Mass spectrometric analytical methods for the determination of endocrine disrupting chemicals (EDCs); Stehmann A et al.; This paper describes a method for the determination of endocrine disrupting chemicals (EDCs) in waste water . The method involves a SPE-C18 extraction followed by a SPE-silica gel column clean up and elution of the analytes with a mixture of acetone/pentane (2+1) . Thereafter derivatisation of the analytes with heptafluorobutyric acid anhydride (HFBA) and analysis by gas chromatography/mass spectrometry (GC/MS) with positive electron impact ionisation (EI) or negative chemical ionisation (NCI) using methane as reactant gas was performed . The two different ionisation techniques were compared and the negative chemical ionisation technique proved significant lower limits of detection (LODs) and quantitation (LOQs) than positive electron impact ionisation . Recoveries of the analytes in various spiked waste water samples ranged from 75.4 to 96.9% . The concentrations of the EDCs in feed waste water from three different waste water treatment plants (WWTPs) ranged from non-detectable up to a concentration of 10,305 ng/L for 4-NP and in the corresponding effluent samples from non-detectable to 723 ng/L for BPA. Water Sci Technol, 2004, 50(5), 141 - 7 Behaviour of bisphenol A (BPA), 4-nonylphenol (4-NP) and 4-nonylphenol ethoxylates (4-NP1EO, 4-NP2EO) in oxidative water treatment processes; Lenz K et al.; Endocrine disrupting chemicals (EDCs) such as natural and synthetic hormones or industrial chemicals can adversely affect the endocrine system at very low concentrations . As such substances can be present in raw water used for drinking-water production, they potentially pose a health risk to humans . In this study laboratory tests were performed to determine removal efficiencies of selected oxidative drinking water treatment processes, namely ozonation (1.4 mg/l O3) and chlorination, using sodium hypochlorite (0.5 mg/l NaClO) and chlorine dioxide (0.4-0.6 mg/l ClO2) under conditions applied in technical plants . 500-300,000 ng/l of bisphenol A (BPA), 4-nonylphenol (4-NP) and 4-nonylphenol-n-ethoxylates (NPnEO) were selected for investigations and measured by HPLC/FLD and HPLC/MS . To investigate possible oxidation by-products, adsorbable organic halogens (AOX) were determined and estrogenic activities were assessed with the help of an estrogen receptor binding assay (YES) . Ozonation and chlorination with ClO2 removed both 4-NP and BPA below detection limits, corresponding with AOX and estrogenic activity . Concerning NPnEO ozonation removed NP1EO and NP2EO up to 28% and 30%, respectively, whereas ClO2 showed high removal efficiencies, eliminating >94% and 92%, respectively . NaCIO removed 4-NP and BPA below detection limits, but estrogenic activities increased and AOX could be measured . NP1EO and NP2EO were only marginally reduced corresponding to the slight decrease of estrogenic potential. Semin Pediatr Infect Dis, 2004 Oct, 15(4), 272 - 9 Vaccines against diarrheal diseases; Nataro JP; At least 2 million persons succumb annually to enteric infection, and in countless other patients, diarrheal disease aggravates malnutrition and susceptibility to other infections . Prevention of enteric illness by virtue of improved hygiene and provision of sanitation and water treatment is impractical in most developing countries, where morbidity and mortality rates are highest . For this reason, development of vaccines against the most important gastrointestinal infections remains a high priority. Water Res, 2004 Nov, 38(19), 4222 - 46 Recent advances in removing phosphorus from wastewater and its future use as fertilizer (1997-2003); de-Bashan LE et al.; Large quantities of phosphate present in wastewater is one of the main causes of eutrophication that negatively affects many natural water bodies, both fresh water and marine . It is desirable that water treatment facilities remove phosphorus from the wastewater before they are returned to the environment . Total removal or at least a significant reduction of phosphorus is obligatory, if not always fulfilled, in most countries . This comprehensive review summarizes the current status in phosphorus-removal technologies from the most common approaches, like metal precipitation, constructed wetland systems, adsorption by various microorganisms either in a free state or immobilized in polysaccharide gels, to enhanced biological phosphorus removal using activated sludge systems, and several innovative engineering solutions . As chemical precipitation renders the precipitates difficult, if not impossible, to recycle in an economical industrial manner, biological removal opens opportunities for recovering most of the phosphorus and beneficial applications of the product . This review includes the options of struvite (ammonium-magnesium-phosphate) and hydroxyapatite formation and other feasible options using, the now largely regarded contaminant, phosphorus in wastewater, as a raw material for the fertilizer industry . Besides updating our knowledge, this review critically evaluates the advantage and difficulties behind each treatment and indicates some of the most relevant open questions for future research. Chlorination remains the most common form of wastewater disinfection in North America due to its low cost and long-term history of effectiveness. One disadvantage is that chlorination of residual organic material can generate chlorinated-organic compounds that may be carcinogenic or harmful to the environment. Residual chlorine or chloramines may also be capable of chlorinating organic material in the natural aquatic environment. Further, because residual chlorine is toxic to aquatic species, the treated effluent must also be chemically dechlorinated, adding to the complexity and cost of treatment. Ultraviolet Light is becoming the most common means of disinfection in the UK because of the concerns about the impacts of chlorine in chlorinating residual organics in the wastewater and in chlorinating organics in the receiving water. Ultraviolet radiation is used to damage the genetic structure of bacteria, viruses, and parasites, making them incapable of reproducing. The key disadvantages of ultraviolet disinfection is the need for frequent lamp maintenance and replacement and the need for a highly treated effluent to ensure that the ultraviolet radiation can get through to any microorganisms present (i.e. solids present in the treated effluent may protect microorganisms from the U.V. radiation). Ozone O3 is generated by passing oxygen O2 through a high voltage potential resulting in a third oxygen atom becoming attached and forming O3. Ozone is very unstable and reactive and oxidizes most organic material it comes in contact with, destroying many disease-causing microorganisms. It has the added bonus of removing other wastewater components such as colour. Ozone is considered to be safer than chlorine because, unlike chlorine which has to be stored on site, ozone is generated as it is required. Sludge treatment The coarse primary solids and secondary biosolids (bacteria) accumulated in a wastewater treatment process must be treated and disposed of in a safe and effective manner. This material is often inadvertently contaminated with toxic organic and inorganic compounds (e.g. heavy metals). The purpose of digestion is to reduce the amount of organic matter and the number of disease-causing microorganisms present in the solids. The most common treatment options include anaerobic digestion, aerobic digestion, and composting. Anaerobic digestion Anaerobic digestion is a bacterial process that is carried out in the absence of oxygen. The process can either be thermophilic digestion (in which sludge is fermented in tanks heated to about 380°C) or mesophilic digestion (cold digestion of sludge where sludge is maintained in large tanks for weeks to allow natural mineralisation of the sludge). Thermophilic digestion generates biogas with a high proportion of methane that may be used to both heat the tank and run engines for other on-site processes. In large treatment plants sufficient energy can be generated in this way to produce electricity for sale. The methane generation is a key advantage of the anaerobic process. Its key disadvantage is the long time required for the process (up to 30 days) and the high capital cost. Aerobic digestion Aerobic digestion is a bacterial process that runs in the presence of oxygen. Under aerobic conditions, bacteria rapidly consume organic matter and convert it into carbon dioxide. Because the aerobic digestion occurs much faster than anaerobic digestion, the capital costs of aerobic digestion are lower. However, the operating costs are characteristically much greater for aerobic digestion because of the need to add oxygen to the process. Composting Composting is also an aerobic process that involves mixing the wastewater solids with sources of carbon such as sawdust or wood chips. In the presence of oxygen, bacteria digest both the wastewater solids and the added carbon source and, in doing so, produce a large amount of heat. Properly designed and controlled, the heat generated can be sufficient to significantly destroy a sufficient number of the disease-causing microorganisms to enable the resulting composted product to be safely used as a soil amendment material (with similar benefits to peat) for agricultural use. Both anaerobic and aerobic digestion processes can result in the destruction of disease-causing microorganisms to a sufficient level to allow the resulting digested solids to be safely applied to land or used for agriculture as a fertilizer provided that levels of toxic constituents are sufficiently low. The choice of a wastewater solid treatment method depends on the amount of solids generated and other site-specific conditions. However, in general, composting is most often applied to smaller-scale applications followed by aerobic digestion and then lastly anaerobic digestion for the larger-scale municipal applications. Sludge Disposal When a liquid sludge is produced, further treatment may be required to make it suitable for final disposal. This includes lagooning in drying beds to produce a cake that can be applied to land or incinerated; pressing, where sludge is mechanically filtered, often through cloth screens to produce a firm cake; or liquid injection to land or liquid disposal to landfill. There are concerns about sludge Incineration because of the contents of the emmissions to air, along with the high cost of supplemental fuel, making this a less attractive and less commonly constructed means of sludge treatment and disposal. Treatment in the receiving Environment Many processes in a wastewater treatment plant are designed to mimic the natural treatment processes that occur in the environment, whether that environment is a natural water body or the ground. If not overloaded, bacteria in the environment will consume organic contaminants, although this will reduce the levels of oxygen in the water and may significantly change the overall ecology of the receiving water. Native bacteria feed on the organic contaminants, and disease-causing microorganisms are reduced by natural environmental conditions that are hostile to these organisms (microbial predation, ultraviolet radiation, etc.) Consequently in cases where the receiving environment provides a high level of dilution, a high degree of wastewater treatment is not necessarily required. However, recent evidence has demonstrated that very low levels of certain contaminants in waste water, including hormones (especially from animal husbandry) and synthetic materials such as pthalates that mimic hormones in their action, can have an unpredictable adverse impact on the natural biota and potentially on humans if the water is re-used for drinking water. However, in nature, microbes live in complex structured communities of diverse, metabolically redundant interacting species, mostly growing as biofilms on surfaces in nutrient-poor, heterogeneous matrices. Most microbes cannot yet be cultivated in the laboratory. The challenge, then, is to exploit cultivation-independent methods to gain a mechanistic understanding of functional relationships in microbial biofilm communities in natural or near-natural settings, to elucidate the rules of microbial behaviour and interactions, and to understand the functional/evolutionary basis of microbial diversity. Genomics has proven to be a powerful, cultivation-independent approach for the characterization of cellular functions and metabolic potential.
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