Disruption of cells in biosolids affects E. coli dynamics in storage

Achieving microbial compliance during biosolids storage can be complicated by the unpredictable increase of Escherichia coli . Thermal treatment during anaerobic digestion (AD) and the effects of dewatering may be a signi ﬁ cant factor contributing to indicator survival. Shear forces present during dewatering may promote cell damage, releasing nutrient for E. coli growth. The effect of cell damage on E. coli survival was assessed in labora-tory-scale thermal and physical disruption experiments. E. coli growth curves for disrupted treatments were compared with control conditions and quanti ﬁ ed using ﬂ ow cytometry and membrane ﬁ ltration techniques. A signi ﬁ cant difference ( p , 0.05) in the level of damaged cells between control and disrupted conditions was observed. For thermal and physical disruption treatments, the peak of E. coli concentration increased signi ﬁ cantly by 1.8 Log and 2.4 Log (CFU (colony forming units) g (cid:1) 1 DS), respectively, compared with control treatments. Research ﬁ ndings contribute to the understanding of bacterial growth and death dynamics in biosolids.


INTRODUCTION
Monitoring levels of pathogenic indicators in biosolids validates the effectiveness of treatment processes and ensures the safe recycling of biosolids to agricultural land (European Commission 2015). Concerns of pathogen removal in biosolids treatment during storage have been raised where post-dewatering levels of microbial indicators can exceed compliance levels (Monteleone et al. 2004;Higgins et al. 2007a;Chen et al. 2011).
Centrifuge dewatering is a common method used to remove the liquid fraction of sludge. Prior to dewatering, Escherichia coli indicator concentrations in the digested liquid sludge tend to be (in the case of study sites examined here) approximately 4 Log (CFU (colony forming units) g À1 DS) (operational data, Severn Trent plc). However, after dewatering operations, particularly in the first 48 h of storage, indicator concentrations have been observed to increase rapidly, reaching levels of approximately 7 Log (CFU g À1 DS) in some cases (operational data, Severn Trent plc). This observation is not isolated and has been observed on other treatment sites (Monteleone et al. 2004;Higgins et al. 2007a;Qi et al. 2007;Chen et al. 2011). This rapid increase in E. coli levels may indicate the presence of pathogenic bacteria within the biosolids product and is a concern for utility operators.
The reasons for indicator increase in stored biosolids post-dewatering have not yet been clearly identified (Dentel et al. 2008). One possible explanation is that following suppression during thermal anaerobic digestion (AD) treatment, the release of readily bioavailable nutrients during mechanical dewatering processes may provide substrates for bacterial growth during subsequent storage periods (Higgins et al. 2006(Higgins et al. , 2007aChen et al. 2011;Sun et al. 2015). The pre-conditioning of the digested sludge with polyelectrolyte to form flocs aggregates the sludge organic matter, which could favour the growth of bacterial cells held within the floc matrix. In addition, the floc structure can provide protection from environmental stressors, prolonging cell survival (Mahendran et al. 2012;Lin et al. 2014).
Although the mechanical dewatering process is conditioned to support aggregation and the formation of the cake product (Higgins et al. 2007b), researchers suggest that the effects of mechanical shear during dewatering treatments can cause floc disruption and even bacterial dispersal, elevating indicator concentrations. Research by Chen et al. (2011) suggested that reasons for the bacterial increase were explained by the release of soluble proteins and other organics during shearing, which serves as substrate sources for microbial organisms. Higgins et al. (2007b) suggested that the cause of indicator increase may be cell reactivation as the shear force exerted on the sludge during centrifuge dewatering releases bioavailable nutrients which supports the culturability of bacterial cells previously held in a viable but non-culturable (VBNC) state. This nutrient release may be from cell lysis. Sun et al. (2015) investigated dewatering processes on cyanobacteria-containing sludge and attributed cell lysis to flocculation turbulence and pressure from mechanical operations on flocs.
The effects of methanogen cell lysis resulting from centrifuge dewatering were studied by Chen et al. (2005) who identified that a higher level of shearing led to greater cell lysis and inhibition of methanogenesis (Chen et al. 2005). The sludge AD environment contains a complex community of bacteria, many of which are obligate anaerobes (Town et al. 2004;Shah et al. 2004). During dewatering, oxygen exposure may be increased in the sludge matrix (Chen et al. 2011), which could additionally have lethal effects on cells preferentially adapted for the anaerobic environment. The growth of E. coli bacteria may, therefore, be enhanced as obligate anaerobes decay and provide a food source for the viable E. coli bacteria to grow.
In response to other stressors such as heat, Noor (2015) identified lysis of VBNC E. coli cells as a response to heat stress. Findings suggested a possible survival output from the cell lysis, contributing to the removal of damaged cells able to serve as nutrients for the remaining population. Research by Higgins et al. (2007b) suggests that the effects of AD cause bacterial cells, including E. coli cells, to enter a VBNC state. The VBNC state of E. coli cells may be reversed during mechanical dewatering as the environment favours the growth of the indicator bacteria. Based on research by Noor (2015), it may be feasible to suggest that a proportion of the bacterial cells in a VBNC state lyse and provide cellular nutrients for the remaining reactivated bacteria. Confirmation of cellular nutrients supporting viable cell survival is highlighted in Murate et al. (2012) who showed that cytoplasmic materials are released into the culture medium as a result of cell lysis and may act as a nutrient supplement for remaining cell population survival. Murate et al. (2012) suggested that further research is required to clarify whether cell lysis increases available nutrients able to support remaining cell survival. The disruption of cells may enhance E. coli replication and the recovery of dormant cells as cellular nutrients are released and added to the sludge matrix. Therefore, the hypothesis tested in this study is that cell disruption provides a substrate source able to support the growth of E. coli bacteria in sewage sludge cake stored under favourable conditions.

METHODOLOGY Sludge sampling and storage
Samples of sludge cake, which had been both mesophilic digested and centrifuge dewatered, were collected from a wastewater treatment works serving a population equivalent of 440,000. The characteristics of the cake at the treatment works showed a sludge of 20% DS with a pH of 8 and a typical E. coli concentration of 5.5 CFU Log 10 g À1 DS at time 0 (day of sample collection). Representative sub-samples were taken to form a bulk sample of approximately 26 kg and were collected at a depth of 0.5 m using a spade or 'corer' device from central locations on the sludge stockpile after the 0.5 m surface 'crust' had been discarded. From this bulk (26 kg) sample, sub-samples were taken for the subsequent experimental treatments. The sludge cake samples collected from the treatment site were less than 24 h old from the point of centrifuge output and enabled laboratory-tested storage environments to begin from 'day 1' assumption. Samples were placed in screw lid sampling pots (Nalgene, Rochester, USA) and transported to the laboratory in insulated cool boxes and stored in the dark at temperatures between 2 and 8°C to suppress biological activity. Samples were processed within 24 h of sampling.
Samples collected from the treatment site were then used in the two sets of experiments described below.

Experimental treatments
To reduce bacterial concentrations, two methods of disruption were applied to samples.

Thermal disruption
Samples of 6 Â 50 g were subjected to treatment at 62°C (+2°C) for 20, 80 and 120 min (Gallenkamp, A. Gallenkamp, London, UK). An additional comparative treatment included 50 g Â 4 samples subject to autoclaving at 121°C for 15 min at 1.03 bar (+0.03 bar) (Priorclave, London, UK). For the experimental set-up, 100 g (2 Â 50 g) of each thermally treated sludge cake sample was placed into a glass beaker (FisherBrand, Loughborough, UK). One (100 g) autoclaved sample was mixed with an additional 0.5 g of the undisrupted sludge cake to reintroduce a sludge-derived bacterial community including E. coli. Alongside the thermal treatments, an undisrupted sample of sewage sludge cake (100 g) was tested as a control condition. All samples were well mixed, covered with Parafilm M ™ (FisherScientific, Loughborough, UK) and stored at 22°C (+2°C) for 10 days. Flow cytometry analysis distinguished intact and damaged cell concentrations and membrane filtration determined E. coli bacterial levels. All sample conditions were repeated in triplicate.

Physical disruption
Microcosms of 3 g of fresh sewage sludge cake sample were mixed with 15 mL of deionised water and sonicated for 7 min at 33 W (MicroTip, Virsonic 600, VirTis, USA). Additional microcosms were set up and not subjected to sonication treatment, remaining as control conditions. All samples were covered with Parafilm M ™ (FisherScientific, Loughborough, UK) and stored at 22°C (+2°C) for 10 days. Flow cytometry analysis distinguished intact and damaged cell concentrations, and membrane filtration determined E. coli bacterial levels. Dissolved organic carbon (DOC) analysis was conducted on samples before and after physical disruption treatment. All sample conditions were replicated in triplicate, and each microcosm was used sacrificially on the day of testing.

Microbial enumeration
Membrane filtration (Environment Agency 2003) was used for bacterial enumeration using Membrane Lactose Glucuronide Agar (MLGA) (OXOID, Basingstoke, UK) plates to distinguish E. coli from coliforms. From each sample condition, 3 g of material was removed and mixed with 15 mL of maximum recovery diluent (MRD) (OXOID, Basingstoke, UK) in a universal tube. To ensure effective homogenisation, samples were subjected to vortexing for 1 min (Scientific Industries Vortex-Genie 2 50 Hz, New York, USA) prior to settling for a further 20 s. The supernatant was then removed for serial dilution. Samples were serially diluted with MRD to ensure CFUs were ,80/plate. Samples were passed through 0.45 µm filters (Millipore S-PAK ® 47 mm, Watford, UK) using a three-way vacuum manifold (CombiSart ® , Sartorius UK Ltd, Surrey, UK). Filters were placed on MLGA plates and incubated at 30°C (+1°C) for 4 h (+1) h and 37°C (+0.5°C) for 18 (+2) h as described by the Environment Agency (2003). Arising green colonies were counted as presumptive E. coli, yellow colonies were counted as coliforms, and pink colonies were recorded as non-coliforms. All E. coli enumeration results were normalised against the percentage of dry solids (DS%). Three gram of the sludge sample was used for DS determination and analysis was performed as per the Environment Agency (2003) guidance.

Flow cytometry measurement
For flow cytometric analysis, 1 g of the sample was vortexed for 30 s with 9 g of MRD to form a liquidsludge mix. Samples were sonicated twice for 2 min (Grant Ultrasonic Bath XUBA1, Grant Instruments Ltd, Cambridgeshire, UK) to enhance the disaggregation of sludge flocs within the sample and disperse bacteria from the sludge particle attachment. Once sonicated, samples were passed through a 20 μm filter (Cat. No. 1004-070, Whatman™, GE Healthcare, Buckinghamshire, UK) using a vacuum pump (N 035.1.2AN.18, KNF Neuberger Ltd, Witney, UK) to remove large sludge particles from the sample, preventing interference with flow cytometry measurement (FCM) (Foladori et al. 2010).
Serial dilution was completed on the prepared sample suspension using filtered, cell-free (0.1 μm; Millex, Merck Millipore Ltd, Tullagreen, Ireland) bottled mineral water (EVIAN, Évian-les-Bains, France), so that the concentration measured with the flow cytometer was always less than 10 6 counts mL À1 . Filtered mineral water is often used as a diluent for flow cytometric analysis as it provides osmotic stability (Hammes et al. 2012;Gillespie et al. 2014).
FCM was completed as described by Gillespie et al. (2014) and Foladori et al. (2007Foladori et al. ( , 2010. SYBR Green I (10,000 Â stock, Cat. No. S-7567, Life Technologies Ltd, Paisley, UK) was diluted with dimethyl sulfoxide (DMSO, Fisher Scientific, Fair Lawn, NJ, USA) to obtain a working stock solution of 100Â. For the measurement of intact and damaged cell concentrations, a dye mix containing five parts of 100 Â SYBR Green I and one part of propidium iodide (PI; 1.0 mg/mL) (Cat. No. P3566, Life Technologies Ltd, Paisley, UK) was prepared. About 2.76 μL of this dye mix was added to 230 μL of the sample. Following the addition of the dye, samples were placed in an incubator shaker (Grant-Bio PHMP, Grant Instruments Ltd, Cambridgeshire, UK) set at 620 rpm at 37°C for 13 min with the lid closed to ensure homogeneous temperature conditions and to avoid light exposure (Gillespie et al. 2014). Following incubation, sample volumes of 50 μL were analysed using a BD Accurri C6 flow cytometer equipped with a 488 nm solid state laser (Becton Dickinson UK Ltd, Oxford, UK).
Green fluorescence was collected in the 'FL-1' channel at 533 nm, and red fluorescence was collected in the 'FL-3' channel at 670 nm with the trigger set on FL-1. Only signals above an FL-1 threshold of 2,000 were recorded. No colour compensation was used. A fixed gate, previously defined by Gatza et al. (2013), was used as a template with the corresponding instrument settings to determine the intact cell concentration (ICC). Data were processed using the Accurri C6 software (Becton Dickinson UK Ltd, Oxford, UK). Damaged cell concentrations were defined by a second fixed gate using the guidance from Foladori et al. (2007Foladori et al. ( , 2010. Figure 1 shows the gate positions used.
All measurements were performed in triplicate and FCM analysis at time 0 was always taken preand post-disruption treatment.
All bacterial numbers, both from membrane filtration and FCM, were referred as the percentage dry solids (DS%) content for normalisation based on Environment Agency (2003) methods.
Dissolved organic carbon analysis DOC determination was conducted using a Series 2000 autosampler (Burkard, Uxbridge, UK) following methods supplied by Burkard Scientific. For sample preparation, 1 g of the sludge cake was vortexed for 30 s with 9 g of deionised water to form a liquid-sludge mix. Samples were sonicated twice for 2 min (Grant Ultrasonic Bath XUBA1, Grant Instruments Ltd, Cambridgeshire, UK) to enhance the disaggregation of sludge flocs within the sample. Once sonicated, samples were passed through a 20 μm filter (Cat. No. 1004-070, Whatman™, GE Healthcare, Buckinghamshire, UK) using a vacuum pump (N 035.1.2AN.18, KNF Neuberger Ltd, Witney, UK) to remove sludge particles. The persulfate ultraviolet oxidation method was used to measure DOC concentrations in the prepared sample (APHA 1995).

Statistical analysis
Using STATISTICA (Version 12, Tulsa, USA), a normality assessment was conducted on the dataset using the histogram and normal probability plot programme function. Variables departing from normality were transformed using a Box-Cox transformation (Marques de Sá 2007). A repeated-measures analysis of variance (ANOVA) was performed to identify statistically significant difference (p , 0.05) between and within the conditions tested. In individual tests, the dependent variable was set as either 'damaged cell concentration', 'E. coli' or 'DOC'. Treatment conditions such as 'undisrupted' and 'disrupted' were set as the categorical factors. The validity of the ANOVA assumptions, including normality of residuals

Thermal disruption
A significant difference was found between levels of damaged bacteria in undisrupted (control) and disrupted treatments (Figure 2). For thermal treatments at 62°C for 80 min, results show a significant increase of 24.7% in the proportion of damaged cells. A gradual increase in damaged cells is observed up to 80 min of exposure. Autoclave treatments showed a significant increase of 36% in damaged cell concentration when compared with undisrupted samples. In comparison with samples exposed to 62°C for 120 min, levels of damaged cells were 11.3% higher in autoclaved treatments. Thermal disruption treatments significantly reduced levels of E. coli bacteria. The greatest reduction was observed after 80 min of exposure where E. coli concentrations fell to 0.8 Log and were significantly different from other treatments at day 1 (Figure 3(b)). In contrast, after 120 min of exposure, E. coli concentrations only showed a reduction to 2.8 Log (Figure 3(c)). For samples exposed to a greater degree of thermal disruption, a longer recovery time was necessary for E. coli populations to return back to pre-disrupted levels or above. Undisrupted samples retained a relatively stable concentration of E. coli, averaging 5.9 Log throughout the 10-day test period.
Thermal disruption of samples consistently resulted in an increase in peak E. coli concentration when compared with undisrupted treatments. A disruption time of 20 min peaked at 7.7 Log, 80 min at 7.2 Log, and 120 min showed a peak E. coli concentration of 7.7 Log. Peak E. coli concentrations for each respective treatment were significantly different (p , 0.05) from undisrupted samples. By day 10, observations of the 20-and 80-min disruption treatments showed a plateau in E. coli concentrations at 7.3 and 7 Log, respectively. This result was significantly higher from the undisrupted sample concentration. For 120 min of exposure, no significant difference was shown with undisrupted samples at day 10.  E. coli concentrations fell significantly to undetectable levels after autoclave disruption (Figure 4(a)). For samples inoculated with 0.5 g of the undisrupted sample after autoclaving, E. coli concentrations were raised to 2.1 Log at day 1. A significant difference (p , 0.05) in peak E. coli concentrations was observed between the two autoclaved treatments. A longer recovery time of 6 days was necessary for autoclaved E. coli populations to return to pre-disrupted levels. Autoclaved treatments showed a steady increase in E. coli concentrations over the test period reaching 6 Log on day 10. For samples inoculated with 0.5 g of the undisrupted sludge, E. coli recovery time was faster and peaked after 3 days at 7.3 Log. A comparison with undisrupted samples showed only the autoclaved treatment with the additional 0.5 g undisrupted sample to have a significantly higher peak E. coli concentration (Figure 4(b)).

Physical disruption
Physical disruption significantly increased the proportion of damaged cells in the sludge sample by 51.6% ( Figure 5). A significant increase of 44,484 mg/kg DS in levels of DOC after physical disruption treatment was observed.   A significant increase of 3 Log was observed in the levels of E. coli bacteria between time 0 and day 3 of storage for physically disrupted samples ( Figure 6). Undisrupted samples remained at a consistent level of 6.6 Log over the 10-day test period. E. coli concentrations in physical disruption treatments increased steadily, peaking at 9 Log on day 4 of storage. The peak E. coli concentration in disrupted samples was significantly different from undisrupted treatments (p , 0.05). Between day 4 and day 10, E. coli concentrations in disrupted samples reduced steadily by 1 Log, despite remaining above control treatment conditions.

Microbial and nutrient response to effects of disruption treatments and growth in subsequent storage
Indicator bacteria increase in stored biosolids has been attributed to the effects of mechanical dewatering. Researchers highlight possible effects of shear impacting upon the integrity of the sludge matrix and causing the release of nutrients, which may support bacterial growth (Higgins et al. 2007b;Chen et al. 2011;Sun et al. 2015). Flocculation turbulence and pressure from mechanical operations on flocs can cause cell damage (Sun et al. 2015). Further to this, researchers have identified cell lysis as a response to mechanical shear and also heat stress factors (Chen et al. 2005;Noor 2015). This research work assessed the impact of  thermal and physical disruption on E. coli behaviour in stored biosolids after initial on-site centrifuge dewatering treatments. Laboratory treatments were conducted as a proof of principle to study the effect of cell disruption on E. coli dynamics and therefore were not intended to replicate on-site biosolids production processes. In order to clarify whether cell disruption increased available nutrients able to support remaining cell survival (Murate et al. 2012), measurements of DOC were undertaken and E. coli enumeration completed in the subsequent days of storage to determine peak concentrations.
Results showed a significant effect of disruption treatment, both thermal and physical, on levels of damaged cells within test samples. Longer exposure to temperature treatments (62°C) and the combination of high temperature and pressure (autoclaving) caused intact cell numbers to fall by 36%. These ICCs were compared with E. coli enumeration data and reflected similar trends with a reduction in levels of culturable E. coli bacteria after thermal disruption treatments. A methodological limitation identified from the thermal disruption treatments was the lower level of E. coli bacteria inactivation identified after 120 min exposure to 62°C where E. coli concentration was only reduced to 2.8 Log. This result was not comparable to the elevated level of cell damage identified in FCM data for 120 min and may have been due to sludge flocs protecting E. coli bacteria and reducing effects from thermal stress (Chang et al. 2001;Qi et al. 2007). The presence of highly aggregated structures or flocs in the tested sludge cake where bacteria may be embedded (Orruño et al. 2013) could protect cells from the 62°C disruption treatment and enable them to remain in a viable state and grow when returned to a lower, more favourable storage temperature (such as the 22°C incubation temperature). Therefore, pre-treatment to disrupt flocs may have been a beneficial stage of sample preparation.
Physical disruption was likely to be more similar to actions experienced in the sludge matrix during mechanical dewatering. Although effects of physical disruption treatments on E. coli were less prominent, FCM data showed damaged cells to increase by 51.6% in tested samples, indicating that other, perhaps more sensitive, sludge-derived bacteria were affected by the treatment. For E. coli concentrations, the reductions displayed after disruption treatments emphasised the inhibition of culturable cells. Though E. coli colonies were reduced on the culture media (in some cases to undetectable levels), this cannot be attributed to cell death and most likely reflect a state of VBNC in cells exposed to disruption treatments. Oliver (2010) suggested that incubation outside of the normal temperature range of growth can induce the VBNC state and is a common response to stress in bacterial cells. This becomes apparent from the E. coli growth curves generated in the following days of storage at 22°C where, in all disrupted treatments, concentrations recovered to pre-disrupted levels. Oliver (2010) studied the effects of temperature on culturability in three strains of Vibrio vulnificus incubated at 11°C to induce a VBNC state (V. vulnificus enters the VBNC state when exposed to temperature ,13°C). After a temperature upshift to 22°C for 24 h, all three strains tested recovered to levels above 10 4 CFU mL À1 (Oliver 2010). The 22°C incubation temperature may have provided an adequate environment for cell reactivation and growth where viable cells could utilise the nutrients released from cells damaged during disruption treatment. Likely evidence of the VBNC mechanism may be identified in autoclave treatments where CFUs reached undetectable levels after treatment but recovered to 2.6 Log within 24 h of incubated storage. A longer storage period may have allowed the peak E. coli concentration to be reached in autoclaved treatments as cell recovery time was slower. However, the significant change in concentration between time 0 and 24 h suggests that cells were able to recover and grow rapidly after such an extreme thermal treatment. Higgins et al. (2007a) highlighted that after dewatering, conditions develop that encourage rapid growth of coliforms with concentrations peaking in 1-3 days of storage. That study attributed reactivation of VBNC cells to shear in mechanical dewatering releasing growth factors which reactivate bacteria to a culturable state (Higgins et al. 2007b). In the present experiments, growth factors such as cellular nutrients have been quantified through the surrogate measure of DOC concentrations. Data showed a significant rise in levels of DOC present in the sludge matrix after disruption treatments (DOC increased by 4,448 mg/kg DS after physical disruption of samples), which coincided with elevated concentrations of E. coli bacteria. This finding is similar to a study by Franz et al. (2008) who found microbial activity per unit of biomass to be positively correlated with concentrations of DOC in manure-amended soils. Natural sources of carbon in sewage sludge will be present in organic compounds (Sigma Aldrich 2016); however, this may not be in a bioavailable form. Carbon is an important component of cellular material (Todar 2012) and, therefore, a critical element required for microbial growth. Tang et al. (2012) observed growth stimulation of E. coli bacteria in assays with DOC-rich samples. In biologically treated sewage effluent, Shon & Vigneswarn (2007) highlighted the constituents of DOC, which included amino acid, polysaccharide and protein. It is likely that the constituents of DOC identified by Shon & Vigneswarn (2007) are also present (perhaps to a more limited extent) in sewage sludge and, therefore, the increase in DOC observed after laboratory disruption treatments is a relevant measure of increasing nutrient levels in the biosolids tested. As sewage sludge cake is known to be nutrient limiting after stabilising up-stream AD processes (Smith et al. 2005), it is likely that any increase in nutrient availability will create a favourable effect on the growth of microorganisms.
In these experiments, physical and thermal stress was imposed on the biosolids material with the aim of increasing cell disruption (lysis), which was quantified using FCM of damaged cells. In the experiments conducted, cell lysis was achieved from the treatments imposed and is verified by the increase in DOC levels in disrupted samples. Shon & Vigneswarn (2007) show DOC to include cell fragment, extracellular enzyme, DNA, RNA and other components of the cellular material. The cellular material from the disrupted cells is able to be used by the remaining cell population to support growth. In the present study, the growth of E. coli bacteria during incubated storage of the disrupted samples consistently showed a significantly higher peak E. coli concentration when compared with undisrupted treatments, indicating an increase in available nutrients for growth.
These findings suggest that cell disruption does provide a substrate source able to support the reactivation and growth of E. coli bacteria in the sewage sludge cake stored at 22°C for 10 days and therefore the hypothesis tested can be accepted.

CONCLUSIONS
1. Thermal and physical disruption treatments were successful methods to increase levels of cell damage within a sample. 2. Increase in damaged cells coincided with higher DOC concentrations indicating cell lysis and an increase in available nutrients for the remaining viable cells. 3. Peak E. coli concentration was significantly higher for disrupted samples in comparison to undisrupted treatments, suggesting the utilisation of cellular nutrients for growth when samples are placed in favourable growth conditions (22°C). 4. The likely release of cellular nutrients from cells damaged during mechanical dewatering may be a contributory factor elevating E. coli concentrations in stored biosolids.