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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 - 436
Nocardia 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 &mdash; 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&ndash;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&ndash;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&ndash;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 . Enzy