Abstract:The objective of this study was to evaluate the effect of solids retention time (SRT) on M. parvicella growth and to calculate growth kinetic parameters of this filamentous species. Bench-scale continuous-flow experiments showed that M. parvicella growth can be significantly suppressed at an SRT of lower than 5.7 d for temperatures of between 14 and 18 o C. According to the continuous-flow experiments the maximum sludge age for the avoidance of filamentous foaming problems caused by M. parvicella is 6 d for te… Show more
“…decreasing mean cell residence time) (Noutsopoulos et al, 2006) additional structures (e.g. classifying selectors) (Chudoba et al, 1973;Caravelli et al, 2003) controlling dissolved oxygen levels in the pre-oxidation reactor (Pasinetti et al, 2005) non-specific measures such as water sprays, steam application (Noutsopoulos et al, 2006).…”
Section: Non Specific Methodsmentioning
confidence: 99%
“…Although the foaming bacteria grow faster on fatty, oily substances, they still grow relatively slowly as the fats, greases and oils are difficult to digest (Griffiths, 2010). It is suggested that the percentage of excessive bulking incidents is 10% to 29% for a SRT of greater than 8.5 d and filamentous bacteria requires a minimum sludge age of 10 days to grow and form a stable population (Griffiths, 2010) whereas there is no bulking occurs for SRTs of lower than 7 d (Noutsopoulos et al, 2006). Most early ASPs were focusing only on the biochemical oxygen demand (removal of organics) and operated at relatively short sludge ages of maximum 3 to 4 days.…”
Section: Causes Of Foamingmentioning
confidence: 99%
“…Specific control strategies are preferable as they are selective and offer a permanent solution of the problem whereas non-specific methods tend to provide only temporary solutions. Noutsopoulos et al (2006), based on laboratory scale studies has shown that reduction of sludge age may prove to be an efficient method to suppress M. parvicella growth. Sludge age reduction method cannot be applied in activated sludge systems that need to nitrify throughout the year, because the sludge age required to washout M. parvicella, may also eliminate nitrifying bacteria.…”
This paper reviews the problem of foaming associated with the activated sludge process and its control using various physical, chemical and biological methods. Activated sludge process is widely used for treatment of every type of wastewater like industrial, domestic and municipal wastewater. This process is driven by a complex microbial population, among which some mycolic acid containing bacteria leads to the stable foam formation which ultimately results in poor efficiency of the plants and leading to major environmental, operational, and health problems. A number of researches provide the evidences of foaming in wastewater treatment plants and its control using physical, chemical and biological methods. Current approaches for controlling foam includes operational adjustments, additional structures, controlling dissolved oxygen levels, water sprays, steam application, polymer addition, chlorination and a novel and ecofriendly approach that is treatment of filamentous bacteria with the specific phages. A detailed study of all methods is presented and collectively described in this review paper for a better understanding of the foam controlling strategies.
“…decreasing mean cell residence time) (Noutsopoulos et al, 2006) additional structures (e.g. classifying selectors) (Chudoba et al, 1973;Caravelli et al, 2003) controlling dissolved oxygen levels in the pre-oxidation reactor (Pasinetti et al, 2005) non-specific measures such as water sprays, steam application (Noutsopoulos et al, 2006).…”
Section: Non Specific Methodsmentioning
confidence: 99%
“…Although the foaming bacteria grow faster on fatty, oily substances, they still grow relatively slowly as the fats, greases and oils are difficult to digest (Griffiths, 2010). It is suggested that the percentage of excessive bulking incidents is 10% to 29% for a SRT of greater than 8.5 d and filamentous bacteria requires a minimum sludge age of 10 days to grow and form a stable population (Griffiths, 2010) whereas there is no bulking occurs for SRTs of lower than 7 d (Noutsopoulos et al, 2006). Most early ASPs were focusing only on the biochemical oxygen demand (removal of organics) and operated at relatively short sludge ages of maximum 3 to 4 days.…”
Section: Causes Of Foamingmentioning
confidence: 99%
“…Specific control strategies are preferable as they are selective and offer a permanent solution of the problem whereas non-specific methods tend to provide only temporary solutions. Noutsopoulos et al (2006), based on laboratory scale studies has shown that reduction of sludge age may prove to be an efficient method to suppress M. parvicella growth. Sludge age reduction method cannot be applied in activated sludge systems that need to nitrify throughout the year, because the sludge age required to washout M. parvicella, may also eliminate nitrifying bacteria.…”
This paper reviews the problem of foaming associated with the activated sludge process and its control using various physical, chemical and biological methods. Activated sludge process is widely used for treatment of every type of wastewater like industrial, domestic and municipal wastewater. This process is driven by a complex microbial population, among which some mycolic acid containing bacteria leads to the stable foam formation which ultimately results in poor efficiency of the plants and leading to major environmental, operational, and health problems. A number of researches provide the evidences of foaming in wastewater treatment plants and its control using physical, chemical and biological methods. Current approaches for controlling foam includes operational adjustments, additional structures, controlling dissolved oxygen levels, water sprays, steam application, polymer addition, chlorination and a novel and ecofriendly approach that is treatment of filamentous bacteria with the specific phages. A detailed study of all methods is presented and collectively described in this review paper for a better understanding of the foam controlling strategies.
“…Indeed, M. parvicella, Type 0092 and Type 0041/0675 are grouped together (Group IV) as aerobic-anoxic-anaerobic-zone growers which are present in conditions of high solids retention, possibly utilising particulate substrates for growth (Martins et al, 2005). Although BNR WWTWs with low F/M ratios, high solids retention times and predominantly particulate and slowly biodegradable COD (SBCOD) have been associated with the selection of Type 0092 (Eikelboom, 2000;Casey et al, 1999aCasey et al, , 1999bCasey et al, , 1999cJenkins et al, 2004;Martins et al, 2003), there is also research which discounts the influence of F/M ratio on the selection process (Noutsopoulos et al, 2006).…”
Section: Eikelboom Type 0092mentioning
confidence: 99%
“…High concentrations of fatty acids are formed when there are long retention times in sewers, primary settling tanks or anaerobic zones, which provide ideal conditions for the proliferation of M. parvicella (Jenkins et al, 2004). Under laboratory conditions, it has been shown that foaming problems due to M. parvicella at low temperatures can be alleviated by reducing the age of the sludge to change the morphology of the filament (Noutsopoulos et al, 2006), and that that the presence of free ammonia as a source of nitrogen can cause bulking by M. parvicella (Tsai et al, 2003). Specific strategies that either have been used (with varying degrees of success) or show promise for the control of filamentous overgrowth of M. parvicella include: reducing solids retention times, using pre-flotation to reduce the lipid fraction, increasing the dissolved oxygen concentration (ideally by employing selectors), and adding polyaluminium hydrochloride (Jenkins et al, 2004;Madoni and Davoli, 2002;Nielson et al, 2002;Roels et al, 2002).…”
Routine characterisation of activated sludge and identification of the filamentous population by microscopic and/or other non-culture dependent techniques can assist in diagnosing the aetiology of poor performance of wastewater treatment works (WWTWs). In South Africa, most facilities rely solely on physicochemical indicators, treating reactors as 'blackboxes', with the result that process adjustments are often delayed, to the detriment of the environment. This study was performed in order to gain insight into the filamentous population found in activated sludge in Cape Town WWTWs, to compare these with other global and local literature findings, and to build capacity in this science. Physicochemical and plant performance parameters, in terms of nutrient removal and settling, were obtained from routine operational data and assessed in conjunction with the microscopic analyses of activated sludge samples taken over a 6-month period. Hypotheses on the links between filament types and/or plant configurations and/or operational parameters were formulated using existing literature. In order of prevalence, the five most common dominant filament species in 96 activated sludge samples were: Eikelboom Type 0092, Eikelboom Type 1851, nocardioforms, Microthrix parvicella and Eikelboom Type 021N. In order to compile a statistically significant database, it is recommended that an extensive nationwide study is conducted to link filament types with plant configurations, operational parameters and geographical locations.
Full-scale demonstration of activated sludge conversion into a granule-floc hybrid process was implemented in Dijon (France) water resource recovery facility (WRRF). Biomass densification was achieved based on external gravimetric selection using hydrocyclones within continuous-flow anaerobicanoxic-oxic (A 2 O) biological nutrient removal (BNR) bioreactor. The goal was to optimize settleability of biological sludge by lowering and stabilizing sludge volume index (SVI) to improve process robustness and resiliency. Process proved to stabilize operation and to uncouple the total solids residence time (SRT) between floc and granule morphologies. The densified biomass initially produced stable SVI < 100 ml/g for a period of 4 months and thereafter a steady state year-round SVI below 50 ml/g, including the winter period during which the control train SVI expansion >200 ml/g. The densified biomass successfully broke the vicious cycle of interannual bulking. Form and function interrelationship is proposed for the densified biomass (hybrid floc-granule).The concept of biological architecture is proposed as the purposeful control of granule and floc proportions, with a proposed "form factor" ratio of 1:2 granule to floc, that produce a "SRT uncoupling function factor" ratio of 4:1 granule to floc, further resulting in very stable settling and effluent functionalities.
Practitioner Points• Controlling granule-floc proportions allows for sludge volume index (SVI) operational adjustment, which further allows for increased clarified design accuracy.• One-third aggregates dramatically improved settling characteristics: 20% and 35% of AGS ensures SVIs below 100 and 50 ml/g, respectively.Sudhir Murthy is a WEF member/fellow. Bernhard Wett is a WEF member.
scite is a Brooklyn-based organization that helps researchers better discover and understand research articles through Smart Citations–citations that display the context of the citation and describe whether the article provides supporting or contrasting evidence. scite is used by students and researchers from around the world and is funded in part by the National Science Foundation and the National Institute on Drug Abuse of the National Institutes of Health.