WASTEWATER TREATMENT PERFORMANCE AND COST DATA TO SUPPORT .

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WASTEWATER TREATMENT PERFORMANCE ANDCOST DATA TO SUPPORT AN AFFORDABILITYANALYSIS FOR WATER QUALITY STANDARDSPrepared for:Michael Suplee, Ph.D.Montana Department of Environmental QualityHelena, MontanaPrepared By:Pamela Hartman and Joshua ClelandICF InternationalLexington, MassachusettsMay 31, 2007

1.0IntroductionThe Montana Department of Environmental Quality (MT DEQ) is currently developingpreliminary, geographically-based nutrient standards for state waters. Some of the preliminarycriteria, which were developed consistent with U.S. Environmental Protection Agency (USEPA)guidance, are low relative to commonly used municipal treatment technologies. Therefore, MTDEQ has initiated an evaluation of the potential economic impacts of the preliminary nutrientcriteria on public and private wastewater treatment entities.MT DEQ began its economic analysis of preliminary nutrient criteria by researching andevaluating existing economic impact assessment methodologies for water quality criteria (ICF2006). That phase of the analysis recommended that MT DEQ develop an affordabilityassessment based on Interim Economic Guidance for Water Quality Standards Workbook(USEPA 1995), which was developed for use by states and USEPA Regions in implementingwater quality standards programs.In the current phase of the analysis, MT DEQ is compiling information about nitrogen andphosphorus reduction technologies for municipal wastewaters. Specifically, this reportsummarizes previously-published information on the performance (e.g., attainable effluentconcentrations of total nitrogen and total phosphorus), availability, technical feasibility, and costof nutrient reduction technologies that may be used at municipal wastewater treatment plants(WWTPs). This information will be used to identify additional treatments and associated costsfor communities of various sizes if the preliminary nutrient criteria were codified.The research methodology used for this report is summarized in Section 2. Section 3 provides adiscussion of nitrogen and phosphorus removal processes and a summary of technologiesconsidered representative of the diverse technologies on the market and that are potentiallyapplicable to small- and medium-sized publicly owned treatment works (POTWs). Althoughmore than 20 relevant information sources on technology performance and costs were identifiedduring research efforts, none provided information that was both comprehensive (e.g., addressingboth phosphorous and nitrogen reduction) and current. However, sufficient information tosupport the MT DEQ affordability assessment can be compiled from key sources (e.g., those thatpresented comparative cost or performance data for multiple technologies). Section 4summarizes the relevant information available in the key sources. In Section 5 providesconclusions and recommendations concerning potential next steps in the affordability analysis.References cited in this report are identified in Section 6.2.0Research MethodologyResearch for this report consisted of a literature search, extensive internet searches, andconsultations with USEPA, state environmental departments, trade organizations, andwastewater treatment technology vendors. Information on technologies was gathered, as well asinformation on performance (e.g., attainable effluent concentrations of total nitrogen [TN] andtotal phosphorus [TP]), technical feasibility, and cost. As available, information was collectedon factors relevant to the MT DEQ affordability analysis, including: (1) relationships betweencommunity size (e.g., population, influent volume) and performance, feasibility, and cost, (2)May 31, 20071

compatibility with other technologies and combined system costs, and (3) regional costinformation relevant to Montana.3.0Nitrogen And Phosphorus Removal Processes3.1Wastewater Treatment ProcessesThe initial stage of wastewater treatment is known as primary treatment, where coarse solids thateasily settle out are removed from the wastewater. Secondary treatment is the second stage inwastewater treatment systems in which bacteria consume the organic material in wastewater.Secondary treatment processes can remove up to 90 percent of the organic matter in wastewaterusing biological processes. The most common conventional methods to achieve secondarytreatment are “attached growth” processes and “suspended growth” processes (USEPA 2004).Attached growth or “fixed film” processes provide a material on which microorganisms attach toform a biofilm. Trickling filters and rotating biological contactors are common aerobic attachedgrowth processes. Suspended growth processes utilize mixing and/or aeration to promote aliquid suspension of the microbial community within a reactor. The most common wastewatersuspended growth process is the activated sludge treatment process. Other process units includeoxidation ditches and sequencing batch reactors (Opus International Consultants Limited 2005;USEPA 2004).Advanced methods of wastewater treatment beyond secondary treatment can be extensions ofconventional secondary biological treatment (as discussed above) to further remove nutrients,such as nitrogen and phosphorus. Advanced treatment may also involve physical-chemicalseparation techniques such as flocculation/precipitation and membrane filtration (USEPA 2004).Some biological treatment processes called biological nutrient removal (BNR) can achievesignificant nutrient reduction, removing both nitrogen and phosphorus. Most of the BNRprocesses involve modifications of suspended growth treatment systems so that the bacteria inthese systems also convert nitrate nitrogen to inert nitrogen gas and trap phosphorus in the solidsthat are removed from the effluent (USEPA 2004). In general, BNR processes are incorporatedinto wastewater treatment systems to reduce effluent TN to an average level of 8 to 10 mg/L andTP to an average of 1 to 3 mg/L before being discharged into a receiving water body (Freed2007). In many cases, BNR technologies can be retrofitted to existing plant configurations andare adaptable to climate extremes. Disadvantages include greater cost than conventionalsecondary treatment, and they also tend to be more sophisticated to operate and require greateroperation training and skill (Hydromantis Inc. 2006). Enhanced nutrient removal (ENR)1 refinesthe BNR process and removes TN to levels as low as 3 mg/L and TP to 0.3 mg/L or less. ENRrelies on the same conventional processes as BNR, with modifications to enhance the microbialactivities to achieve higher levels of efficiencies and greater reductions in nitrogen andphosphorus (Freed 2007).1Various names and acronyms are used in the literature for related biological treatment processes. For example,ENR is sometimes referred to as enhanced biological nutrient removal (EBNR). ENR specifically for phosphorusremoval may be referred to as enhanced biological phosphorus removal (EBPR). This report generally uses processnames and acronyms used in cited publications.May 31, 20072

3.2Nitrogen Removal in WastewaterNitrogen in wastewater is generally in the form of ammonia and organic nitrogen (GMB 2004).Nitrogen in municipal wastewater is usually not removed by conventional secondary treatment.BNR for nitrogen is achieved through a series of biochemical reactions that transform nitrogenfrom one form to another. The key transformations are nitrification and denitrification (USACE2001). By providing additional biological treatment beyond the secondary stage, nitrifyingbacteria present in wastewater treatment can biologically convert ammonia to the non-toxicnitrate through the process known as nitrification. The nitrification process is normally sufficientto remove the toxicity associated with ammonia in the effluent. An additional biological processcan be added to the system to convert the nitrate to nitrogen gas. The conversion of nitrate tonitrogen gas is accomplished by bacteria in the process known as denitrification. Effluent withnitrogen in the form of nitrate is placed into a tank devoid of oxygen, where carbon-containingchemicals, such as methanol, are added or a small stream of raw wastewater is mixed in with thenitrified effluent. In this anoxic environment, bacteria use the oxygen attached to the nitrogen inthe nitrate form releasing nitrogen gas into the atmosphere (USEPA 2004).3.3Phosphorus Removal in WastewaterPhosphorus removal obtained in a conventional biological wastewater treatment is generally lessthan 20 percent. Because it is not possible to achieve low phosphorus effluent limits withconventional biological wastewater treatment processes, additional or alternative treatmentmethods must be employed (Park et al. 1997). Phosphorus can be removed through chemicalprecipitation, physical processes (using filtration and membrane), or by a process calledenhanced biological phosphorus removal (EBPR). Chemical precipitation, which is alsocommonly referred to as chemical addition or flocculation, can be achieved through addition ofalum, lime, or iron salts to the wastewater. With these chemicals, the smaller particles ‘floc’ orclump together into large masses that settle faster when the effluent reaches the sedimentationtank. This process can reduce the concentration of phosphate by more than 95 percent. Thelevel of phosphorus removal achieved by chemical precipitation can be controlled bymanipulating the amount of chemical added. This process produces a chemical sludge, and thecost of disposing this material can be significant (USEPA 2004).EBPR methods provide a number of advantages over chemical addition including improvedtreatment, reduced chemical usage, reduced energy consumption, reduced sludge production, andimproved sludge settling and dewatering characteristics (Park et al. 1997). EBPR typicallyinvolves an activated sludge process modification (alternating aerobic and anaerobic and anoxicconditions) that allows for a high degree of phosphate removal from wastewater, with thepotential to achieve very low ( 0.1 mg/L) TP (Strom 2006).Table 1 provides information on select nutrient removal technologies considered representativeof the diverse technologies available and that are potentially applicable to municipal wastewatertreatment facilities in Montana.May 31, 20073

Table 1. Selected Nutrient Removal ProcessesProcessProcess DescriptionNutrientRemovedSources forAdditionalInformationBiologicalSuspended Growth (Activated Sludge)Bacteria kept in suspension to allow bacteria to grow and consume pollutants from wastewater2-step nitrification/denitrification process.Hatch MottLudzack EttingerNMacDonaldundated;Anoxic/aerobic2-step nitrification/denitrification process with internalHatch MottModified Ludzackrecycle.NMacDonald undated;Ettinger (MLE)GMB 2004Anoxic/aerobic4-step process designed to achieve completedenitrificationHatch MottAnoxic/aerobic/anoxic/aerobic4-Stage BardenphoNMacDonald undated;GMB 2004Most commonly used activated sludge process that hasconsistently demonstrated the ability to meet ENRgoals for TN.Adds an aerobic zone to the 4-stage Bardenpho toHatch Mottachieve P removal5-Stage BardenphoN&PMacDonald undated;GMB 2004Anaerobic/anoxic/aerobic/anoxic/aerobicLooped channel reactor, with aerobic and anoxic zonescreated around the channel; forUSEPA 2000c; Hatchnitrification/denitrification; utilizes long solidsOxidation DitchNMott MacDonaldretention times to achieve a high degree ofundated; GMB 2004nitrification; an anaerobic tank may be added prior tothe ditch to enhance biological P removal.Consists of suspended growth basins wheremembranes are employed for suspended solidsseparation prior to effluent discharge; allows for theMembrane Bioreactorestablishment of processes with extended residenceHydromantis Inc.N(MBR)2006; Peterson 2006times; facilitates biodegradation of substances that arefacilitated by slow-growing microorganisms; allowsclarification, aeration, and sludge digestion in oneprocess step.For nitrification/denitrification; creates anoxic andUSEPA 2004;aerobic conditions at timed intervals for biologicalUSEPA 1999; HatchSequencing Batch ReactorNtreatment and secondary clarification in a singleMott MacDonald(SBR)reactor; cycles within the system can be easilyundated; GMB 2004;modified for nutrient removal.Peterson 20062-step nitrification/denitrification process with internalrecirculation. Good P removal may be achieved if theTwo-stage ActivatedPJiang et al. 2004nitrate concentration is at low enough levels.Sludge (AO)Anoxic/aerobicSimilar to the MLE process, except that an anaerobicThree-stage ActivatedGMB 2004; Jiang etzone is included for P removal.N&PSludge (A2O)al. 2004Anaerobic/anoxic/aerobicUses 4 separate process zones to remove N and P; thefirst anoxic zone is used to remove nitrate and oxygenJohannesburgN&PGMB 2004and set up anaerobic conditions; the remainder of the2process is similar to A O.May 31, 20074

Table 1. Selected Nutrient Removal ProcessesProcessProcess DescriptionNutrientRemovedSources robicAttached Growth (Fixed Film)Utilizes media to provide a surface for biomass to grow and perform nitrification & denitrificationFor nitrification/denitrification; involves a tank,USEPA 2000d;usually filled with a bed of rocks, stones or syntheticTrickling FilterNUSEPA 2004;media, to support bacterial growth used to treatUSACE 2001wastewater.Rotating BiologicalFor nitrification/denitrification; series of disks attachedGMB 2004; USACEContactorto a central axis that rotates and exposes biomass onNdisks to both air (aerobic conditions) and wastewater2001; Peterson 2006(anoxic conditions).Denitrification FilterUtilize granular media to remove nitrates afternitrification. May be added to existing treatmentHatch Mottsystems that use biological processes to convertNMacDonald undated;nitrate-N to N gas; physical/chemical treatment mayFreed 2007be added using chemical phosphorus precipitation toachieve TP as low as 0.3 mg/L.Fluidized Bed ReactorFor nitrification/denitrification; utilizes small mediawhich is kept in suspension by aeration or mixingNGMB 2004action; aerobic and anaerobic reactors may be arrangedin series for complete BNR OR may be added to anexisting BNR process for additional denitrification.Assimilation (Aquatic)Utilizes aquatic plants for nutrient assimilation, transfer of oxygen, and improved water qualityConsist of a series of ponds that contain cultivatedplants of some type; remove nutrients such as P and Nby plant uptake; suspended solids may be removed bysedimentation and filtration processes. Althoughavailable sources (e.g., USEPA 2000a; USEPA 2000f)Hydromantis Inc.Constructed Wetlandprovide contradictory conclusions about theN&P2006; USEPA 2000a;(Surface)effectiveness of this method for removing P and N,USEPA 2000fdesign and operation modifications (e.g., increasedretention times) can produce N and P removal.Because winter weather hinders wetland processes,lagoon wastewater storage may be required duringcold months.Constructed WetlandConsist of a porous media (e.g., gravel) through which(Subsurface)the wastewater is directed; plants are often grown inthe media to facilitate oxygen transfer into thesubsurface and promote aerobic conditions; facilitateHydromantis Inc.suspended solids removal through sedimentation andN&P2006; USEPA 2000b;filtration mechanisms. Comments about theUSEPA 2000feffectiveness and limitations surface constrictedwetlands (above) also apply to subsurface constructedwetlands.Wastewater treatmentConstructed pond that allows sunlight, algae, aerobicpond/lagoonand anaerobic bacteria, and oxygen to interact toUSEPA 2002a;Nimprove water quality; may be used for secondaryUSEPA 2004treatment or as a supplement to other processes.Removes biodegradable organic material and some ofMay 31, 20075

Table 1. Selected Nutrient Removal ProcessesProcessProcess DescriptionNutrientRemovedSources forAdditionalInformationPUSACE 2001PHydromantis Inc.2006PUSEPA 2000e;Hydromantis Inc.2006the N from wastewater, but only in moderate amounts.Lagoon operation is significantly impacted by winterweather.PhysicalReverse OsmosisSand FiltrationPerforms micro-filtration processes using membrane;will remove nearly all particulate P and 95-99%soluble P; membrane treatments may be expensive.Traps some solids remaining in the wastewater aftersecondary treatment. Can reduce P adsorbed to solidparticles, such as particles remaining in suspensionafter chemical addition (see below). In some cases,biological nitrification/denitrification is also achievedwith sand filters. Performance may be adverselyaffected by cold weather.ChemicalChemical Addition4.0Also commonly referred to as chemical precipitationor flocculation. Metal salts (e.g. alum, iron) or otherchemicals may be used as coagulants and precipitatingagents to enhance the formation and separation ofsolids that can removed from wastewater stream.Chemicals are added to either a conventionalsecondary treatment process (e.g., activated sludge) ormay be incorporated as part of a tertiary treatmenttechnology (e.g., sand filtration); the effectiveness ofthe agent will be a function of the solids separationefficiency and its effectiveness in forming a solidassociated contaminant.Summary of Key ReferencesThis section summarizes the most relevant and potentially useful sources of cost andperformance data identified from literature searches and other information gathering. Thefollowing factors were considered in choosing the most relevant and potentially useful sources: Year of publication – Recent publications are more likely than older publications topresent current cost information and state-of-the-art processes and performance.Accepted or demonstrated technologies – Publications about experimental treatmentprocesses were considered less relevant than case studies and other publications aboutaccepted treatment methods.Comparative analysis – Many variables (e.g., year, waste stream characteristics) affectthe cost and performance of wastewater treatment processes. Comparative analyses, inwhich the outcomes of alternative treatment scenarios or effluent limitations arecompared, provide insights about the relative advantages and disadvantages oftechnologies.May 31, 20076

4.1Cost curves or scaling information – Some sources present cost curves or otherinformation describing the relationships between design capacity and cost. Theserelationships may be based on data from a sample of facilities with similar configurationsor from detailed engineering and cost calculations for a various design capacities.Case studies – Case studies generally include important details about the advantages anddisadvantages of the available technologies. In addition, case studies are more likely thanguidance documents, cost estimation studies, and other types of references to provideactual, post-construction cost and performance information.Advanced Wastewater Treatment to Achieve Low Concentrations ofPhosphorus (USEPA 2007)USEPA Region 10 compiled performance and cost data from 23 municipal WWTPs withadvanced phosphorus reduction technologies. This report (i.e., USEPA 2007) documents thelevels of phosphorus control attainable by current technologies and certain combinations oftechnologies. The report presents total residential sewer rates, but no cost data specific tophosphorus reduction.Phosphorus reduction technologies used at the WWTPs studied by USEPA included chemicaladdition, ENR, and various filtration technologies. All but one of the WWTPs employs tertiaryfiltration aided by chemical addition. Monitoring data from these WWTPs shows that thiscombination of technologies can consistently achieve an effluent phosphorus concentration of0.01 mg/L.All of the WWTPs studied by USEPA used some form of filtration (e.g., traveling sand bedfiltration, mixed-media gravity filtration, Dynasand filtration). Facilities with the lowestreported phosphorus concentrations (i.e.,

Secondary treatment is the second stage in wastewater treatment systems in which bacteria consume the organic material in wastewater. Secondary treatment processes can remove up to 90 percent of the organic matter in wastewater using biological processes. The most common conventional methods to achieve secondary treatment are “attached growth .

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