Användandet av obehandlat avloppsvatten inom jordbruket är en växande företeelse i många delar av världen. Speciellt i vattenfattiga områden där avloppsvattnet ses som en värdefull och pålitlig resurs. Det höga näringsinnehållet minskar behovet av konstgödsel och detta ökar böndernas inkomster. Men med användandet av avloppsvattnet följer vissa hälsorisker. Bland annat har man sett en högre förekomst av inälvsmaskar hos bönder som använder orenat avloppsvatten jämfört med de som använder rent vatten. Den här vattenkvalitetstudien har utförts längs floden Musi i Andhra Pradesh, Indien. Musi rinner igenom staden Hyderabad och mycket av stadens avloppsvatten dumpas i floden. Nedströms Hyderabad används detta vatten för bevattning. Längs med floden är dammar byggda, för att avleda vattnet i bevattningskanaler. Reservoirer bildas då flödeshastigheten minskar. Studieområdet sträcker sig från Hyderabad och 28.7 km nedströms. Hypotesen var att reservoirerna fungerar som biodammar och syftet var att kvantifiera dammarnas inverkan på vattenkvaliteten och utvärdera dess lämplighet utifrån ett hälso- och jordbruksperspektiv. Inom studieområdet är reningen med avseende på BOD, Nematoder och E coli 86,9%, 99,9% respektive 99,9%. Trots att reningen är så hög överstiger Nematod- och E coli-koncentrationerna Världshälsoorganisationens riktlinjer och utgör en hälsorisk för bönder och konsumenter. Syre- och salthalt ökar nedströms och den höga salthalten kan ha negativ inverkan på jordbrukets avkastning. Genom att titta på reningsmönster och förändring av olika vattenkvalitetsparametrar är en av slutsatserna av detta arbete att reningen i dammarna motsvarar den rening som sker i de anaeroba bassängerna i ett biodammsystem. / The use of untreated domestic sewage in agriculture is a growing practice in many parts of the world. It is being looked upon as a valuable and reliable resource in water scarce communities. Wastewater is usually rich in nutrients and the use results in high yields without the need for artificial fertilisers. But with the use of untreated wastewater follows a number of associated health risks, e.g. a higher prevalence of helminth infections has been seen among wastewater users compared to non-users. This water quality study was performed along the River Musi in Andhra Pradesh, India. The Musi River flows through the city of Hyderabad carrying the most of the town’s wastewater. Downstream of Hyderabad the wastewater is used by farmers for irrigation. Along the river weirs are constructed which diverts the irrigation water into canals and reservoirs are formed where the flow velocity slows down. The study area stretches from Hyderabad and 28.7 km downstream. The hypothesis was that the existing irrigation infrastructure acts like Wastewater Stabilisation Ponds and the aim was to quantify the impact of the weirs on water quality and to evaluate the irrigation water quality in reference to associated health risks and agricultural suitability. Within the study area the BOD, E coli and Nematode removals were 86.9%, 99.9% and 99.9% respectively. Despite the high removal the E coli and Nematodes, the concentrations exceed WHO guidelines for unrestricted and restricted irrigation, and there exists an excess risk of intestinal nematode- and enteric infections for farmers. Dissolved oxygen and salinity increases downstream and due to the high salinity farmers could experience reduced crop yields. By looking at removal patterns, and the change in water quality parameters, the conclusion can be made that the reservoirs act like anaerobic ponds in a Wastewater Stabilisation Pond system.

För att simulera aktivslamprocessen på ett reningsverk krävs en dynamisk modell som realistiskt beskriver processen. 1987 kom IWA, International Water Association med ASM1, Activated Sludge model no. 1 som fortfarande är den mest använda modellen för att beskriva denna process. I detta examensarbete har ASM1 används för att beskriva aktivslamprocessen på Henriksdals reningsverk i Stockholm. Arbetet har utförts som en del i ett europeiskt projekt, HIPCON (Holistic Integrated Process CONtrol) på IVL, Svenska Miljöinstitutet AB. Arbetet har gått ut på att ta fram en modell som realistiskt beskriver aktivslamprocessen och eftersedimenteringen. För att göra detta har en referensmodell i MATLAB/Simulink använts som grund och byggts om för att likna processen vid Henriksdal. Denna modell i Simulink använder ASM1 för att beskriva aktivslamprocessen. Eftersedimenteringen modelleras med en massbalansmodell där sedimenteringshastigheten beskrivs av en dubbelexponentiell sedimenteringsfunktion. Både ASM1 och sedimenteringsfunktionen använder en mängd olika parametrar för att beskriva processerna och dessa måste kalibreras fram för den process som skall modelleras. Aktivslamprocessen är en biologisk process som beror på en mängd yttre och inre faktorer och är unik för varje reningsverk. Därför finns det inte något enkelt sätt att kalibrera en modell på och information för det enskilda reningsverket i fråga måste tas fram. I detta arbete har två mätkampanjer utförts på Henriksdal för att få mätserier till kalibrering och validering samt information om avloppsvattnets sammansättning. Litteraturstudier har också genomförts för att få information om vilka parametervärden som är av störst intresse för modellen samt i vilket område varje parameter kan förväntas finnas. Arbetet har sedan gått ut på att efter riktlinjer för kalibrering funna i litteraturen ta fram en modell som så realistiskt som möjligt beskriver processen på Henriksdal. Först genomfördes en kalibrering med medelvärden för att hitta jämviktstillstånd och därmed en stabil modell på länge sikt. Utifrån den modellen utfördes sedan en dynamisk kalibrering för att få en modell som beskriver även kortsiktiga och snabba förändringar. Till sist utfördes en validering för att kontrollera om modellen fungerar även för en dataserie som ej använts vid kalibrering. Den framtagna modellen fungerade mycket bra för att modellera medelvärden på lång sikt. För snabba förändringar verkade modellen ligga fel i tiden och troligtvis var den reella uppehållstiden kortare än den teoretiska och bidrar till sämre modellanpassning. / To simulate the activated sludge process at a wastewater treatment plant a dynamic model that describes the process is needed. In 1987 IWA, International Water Association presented ASM1, Activated Sludge Model No.1 which still is the most widely used model for this process. In this thesis the ASM1 has been used to describe the activated sludge process. The work is a part of a European project, HIPCON (Holistic Integrated Process CONtrol) at IVL, Swedish Environmental Research Institute. The main objective of the work was to calibrate a model that realistically describes the activated sludge process and secondary sedimentation at Henriksdal wastewater treatment plant in Stockholm. A benchmark model in MATLAB/Simulink was used as a base and rebuilt and extended to fit the process of Henriksdal. In the model ASM1 is used to describe the activated sludge process. The settler is modelled with a mass balance model where the settling velocity is described by a double exponential function. The parameters used in both models have to be calibrated to fit the wastewater treatment plant. To find information about Henriksdal two measuring campaigns were performed to provide data for calibration and validation and to gather information about the composition of the incoming wastewater. From this data a model was developed and calibrated for the process at Henriksdal. After calibration the obtained model worked very well for modelling average values but did not adjust quite as well to fast dynamic changes.

Hedesunda reningsverk är beläget i södra delen av Gävle kommun och hanterar avloppsvatten från Hedesunda samhälle och ett fåtal närbelägna byar. Antalet anslutna personer är strax över 1500. Reningsverket byggdes på 1960-talet och byggdes om i slutet av 1990-talet. Vid ombyggnaden anlades torkbäddar för avvattning av det slam som produceras vid reningsverket. Inledningsvis fungerade dessa torkbäddar bra men sedan 2005 har slammet i bäddarna inte avvattnats i önskad omfattning.   Syftet med detta examensarbete var att utreda hur slamavvattningen i Hedesunda ska se ut i framtiden. Utgångspunkten var att den nuvarande lösningen är otillräcklig och att en förändring är nödvändig. Inledningsvis delades frågeställningen upp i två separata delar: avvattning av slammet och avsättning för avvattnat slam. Fokus låg på ekonomiska och miljömässiga aspekter av slamhantering och en sammanvägning av dessa gjordes där så var möjligt.   Frågan om hur avvattningen bör se ut undersöktes genom att en enkät skickades ut till nio olika företag som levererar avvattningsutrustning. Dessa fick svara på 17 frågor om vilken lösning de ansåg vara bäst lämpad för reningsverket i Hedesunda. Sammanlagt samlades sex olika svar in. Utöver dessa undersöktes även alternativet att restaurera de befintliga torkbäddarna närmare. Detta skedde bland annat genom provtagning och analys av slammet i bäddarna. De olika alternativen för slamavvattning sammanställdes och jämfördes genom att varje undersökt parameter delades in i intervall som gav olika betyg. De tre alternativ som enligt denna undersökning ansågs bäst lämpade var att restaurera de befintliga bäddarna, att anlägga vassbäddar eller att installera en mindre silbandpress.   Då slammet avvattnats återstår frågan kring hur det avvattnade slammet ska hanteras. Detta undersöktes genom att två alternativ studerades närmare. Dessa var att fortsätta med den nuvarande hanteringen som är kompostering och tillverkning av anläggningsjord eller att certifiera slammet genom REVAQ och sprida det på åkermark. Ett försök till att skatta kostnaden för de båda alternativen gjordes, bland annat genom att frågor ställdes till de kommuner/driftbolag som idag är certifierade enligt REVAQ. Kostnaden för certifiering och spridning på jordbruksmark är betydligt mycket högre än kostnaden för kompostering. Certifieringsalternativet innebär dock en större måluppfyllelse i och med att fosfor återförs till produktiv mark.      Resultatet av studien är ett konkret förslag på hur slamavvattning och avsättning för slam vid Hedesunda reningsverk kan skötas i framtiden. Detta förslag innebär att de nuvarande torkbäddarna restaureras och att möjligheterna att certifiera flera delar av Gästrike Vatten AB:s verksamhet utreds närmare. Att enbart certifiera slam från Hedesunda reningsverk anses ekonomiskt orimligt. / Hedesunda wastewater treatment plant (wwtp) is located in the southern part of Gävle municipality in Sweden. The wwtp treats wastewater from Hedesunda community and a few nearby villages. All in all there are approximately 1500 persons connected to the plant. Hedesunda wwtp was originally built in the 1960’s and was restored in the late 1990’s. At the restoration sludge drying beds were built on the site for sludge dewatering. Initially, these beds worked fine but since 2005 the dewatering result has not been satisfactory.   The objective of this master thesis has been to investigate different alternatives for a more effective sludge handling at Hedesunda wwtp in the future. Initially the sludge handling process was divided into two different parts: sludge dewatering and management of dewatered sludge. The focus has been on economical and environmental aspects of sludge handling and where it’s been possible these factors have been weight together.   The question of how a more effective dewatering of sludge could be achieved was answered by a questionnaire that was sent to different companies that supply dewatering equipment to the Swedish market. Altogether six answers were collected. Besides these answers the option of restoring the existing sludge drying beds was also considered. The latter was done by sampling and analyzing sludge in the existing beds, among other things. The different options for dewatering were compiled and compared in a matrix where every parameter was split up in intervals and assigned grades. Three options that received the highest total grade were considered the best options. These were: restoring the sludge drying beds, reed beds and a small belt filter press.   The matter of how to handle the dewatered sludge was simplified to a study of only two alternatives. These were to continue the present handling or to certify the sludge according to REVAQ and use it as fertilizer. Attempts to estimate the cost for the two alternatives were made. The cost for certification is higher than the cost for composting, but to certify the sludge will lead to a higher target achievement.   The study resulted in concrete suggestions for how the sludge at Hedesunda wwtp can be handled in the future. This suggestion states that the existing sludge drying beds should be restored and that the possibility to certify several wwtp:s within Gästrike Vatten AB should be investigated. It is not considered economically plausible to certify sludge from Hedesunda wwtp alone.

In this report, the application of Principle Component Analysis (PCA) and Partial Least Square (PLS)  regression analyzing methods used to understand the relationship of interdependent loads in municipal wastewater treatment plant. Two different wastewater treatment plants were chosen for analysis of  the relationship between interdependent loads. Firstly, the collected data of incoming wastewater and outgoing water from both Västerås and Eskilstuna wastewater treatment plants were analyzed to find some relationship or correlation between contents and compare the data of both the plants. Secondly, the correlated contents were used to generate the regression model for predicting the value in the future, in this report we have focussed only on ammonium nitrogen value for regression model. The PCA study shows the variation between incoming and outgoing wastewater’s characteristics  given by  Västerås and Eskilstuna plant. / BOD, ammonium nitrogen, nitrogen, phosphorus

Within this study it was investigated how much energy and money that could be saved by implementing new aeration equipment and aeration control in Sternö wastewater treatment plant (WWTP). Sternö WWTP is a full-scale plant built in 1997 and dimensioned for 26 000 population equivalents. The plant has two parallel biological treatment lines with pre-denitrification. During the study, one of the treatment lines was used as a test line, where new aeration equipment and control was implemented. The other line was used as a reference line, where the aeration equipment and control was maintained as before. The new aeration equipment that was implemented to support the test line was an AtlasCopco screw blower, fine bubble Sanitaire low pressure diffusers and measurement equipment. Two control strategies were tested: oxygen control and ammonium control. The results show that 35 percentage points of the test line energy consumption was reduced with the new screw blower. The diffusers saved another 21 percentage points and by fine tuning the controllers, the oxygen concentrations and the air pressure a further 9 percentage points could be saved. The ammonium control gave no energy savings, since the lowest allowed DO set-point (0.7 mg L-1) kept effluent ammonium below the ammonium set-point of 1 mg L-1.  The final energy savings of the test line was 65 ± 2 %. Each aeration equipment upgrade increased the energy savings with: •    Blower 35 %. •    Diffusers 32 %. •    Oxygen control with decreased DO concentrations and air pressure 21 %. The final savings correspond to 13 % of the total energy consumption of Sternö WWTP. These savings are equivalent to annual savings of 178 MWh, which decreases the energy costs by 200 000 SEK per year. The payback period of the implemented aeration equipment and control was 3.7 years. / I denna studie har det undersökts hur mycket energi och pengar som kan sparas genom att installera ny luftningsutrusning och luftningsreglering i Sternö avloppsreningsverk. Reningsverket är beläget i Karlshamn och dimensionerat för 26 000 personekvivalenter. Den biologiska reningen är uppdelad på två parallella reningslinjer, där den ena användes till försök och den andra som referenslinje i denna studie. Den biologiska reningen utgörs av en konventionell aktivslamprocess med fördenitrifikation. Studien innefattade en simulering där två olika reglerstrategier för luftningen jämfördes. Simuleringen gjordes i programmet Benchmark Simulation Model no 1 och modellen anpassades för att efterlikna Sternö reningsverk på bästa sätt. De två reglerstrategierna för luftningen utgjordes av luftstyrning baserad på syrekoncentration i bioreaktorerna och luftstyrning baserad på utgående ammoniumkoncentration från bioreaktorerna. Simuleringen visade att energibesparingen från ammoniumreglering jämfört med en syrereglering är liten. Fördelen med ammoniumreglering är istället att den önskade reningsgraden lättare kan uppfyllas över året, trots varierande temperatur. Vid fullskaleförsök vid försökslinjen installerades ny luftningsutrustning (AtlasCopco blåsmaskin med skruvteknologi, Sanitaire småbubbliga diffusorer, samt mätnings-utrustning) och ny luftstyrning. Två luftstyrningsstrategier testades: syrereglering och ammoniumreglering. Resultaten visade att blåsmaskinen gav en energibesparing på 35 procentenheter, att diffusorerna gav en energibesparing på 21 procentenheter och att fininställd syrereglering tillsammans med sänkta syre- och lufttrycksnivåer gav en sänkning på 9 procentenheter. Ammoniumregleringen gav ingen energibesparing eftersom den lägst tillåtna syrekoncentrationen (0,7 mg L-1) höll ammonium-koncentrationen under sitt börvärde på 1 mg L-1. Den slutliga energibesparingen för testlinjen var 65 ± 2 %. Varje luftningsutrustning bidrog med följande energibesparing: •    Blåsmaskin 35 %. •    Diffusorer 32 %. •    Ny syrereglering med sänkta syre- och lufttrycksnivåer 21 %. Den slutliga energibesparingen i testlinjen motsvarar 13 % av Sternö reningsverks totala energiförbrukning, vilket gör att 178 MWh kan sparas per år. Den minskade energi-förbrukningen sänker energikostnaden för reningsverket med 200 000 SEK per år. Återbetalningstiden på den till försökslinjen installerade utrustningen var 3,7 år.

Microbial fuel cells were designed and operated using waste activated sludge as a substrate and as a source of microorganisms for the anodic chamber. Waste activated sludge provided a bacterial consortium predisposed to the solubilization of particulate matter and utilization of substrates commonly found in wastewater. Dissolved oxygen and ferricyanide were used as the electron acceptors in the catholytes. Microbial fuel cell comparisons were made while operating under identical conditions but using the two different electron acceptors. Comparisons were based on the electricity production observed during MFC operation, wastewater quality of the waste activated sludge anolytes and the community level physiological profiling of the microbial communities in the anolytes. Electrons liberated during substrate utilization in the anodic chamber traveled to the cathodic chamber where they reduced the electron acceptors. The anode and cathode chambers were connected by a Nafion ® proton exchange membrane to allow for cation migration. Various soluble carbon sources were dosed to the microbial fuel cells at measured intervals during operation via direct injection to the anolyte. During bovine serum albumin dosing, average power production levels reached 0.062 mW and 0.122 mW for the dissolved oxygen microbial fuel cell and the ferricyanide microbial fuel cell, respectively. These were 100% and 25% greater than the power production levels observed throughout the rest of the study. Increases in current production were observed following the dosing of sodium acetate, glucose and bovine serum albumin. No increase in current was observed following glycerol dosing. Sodium acetate dosing triggered an immediate response, while glucose and bovine serum albumin responded in approximately 2 minutes. A chemical oxygen demand mass balance was calculated for both microbial fuel cells. The lack of balance closure was attributed to unmeasured methane production. An accumulation of particulate waste activated sludge components was observed for both microbial fuel cells. The anolyte pH during operation was typically less than waste activated sludge pH, which was attributed to volatile fatty acid accumulation in the anolytes during fermentation processes. Community level physiological profiling was accomplished through the analysis of ecological data obtained with BIOLOG ® ECOplates. Samples were plated and analyzed under anaerobic conditions, mimicking the environment in the anode chamber of the MFCs. ECOplate data were transformed by a logarithmic function prior to principle component analysis. The community level physiological profiling indicated that shifts in the microbial community profile, as measured through the carbon source utilization patterns, occurred throughout acclimation and following the dosing of various carbon source substrates. Shifts due to glycerol dosing differed from shifts due to the dosing of sodium acetate, glucose and bovine serum albumin.

This thesis is an investigation of landscape as boundary: a study of its formation, inhabitation, and symbolic meaning. The study is situated in a valley located south of Jerusalem’s Old City walls; known as both Gei Ben-Hinnom and Wadi al- Rababa, it is an ethnic, cultural, socioeconomical, and mythological boundary. In the ethnically polarized Jerusalem, valleys often act as boundaries between Jewish and Palestinian populations. For nineteen years an official no-man’s-land divided the Hinnom/Rababa Valley, a result of an armistice agreement between Israel and Jordan. Since the 1967 annexation of East Jerusalem to Israel, the valley has transformed into a boundary between the two populations. Responding to this boundary, the thesis addresses an urgent need for a wastewater treatment facility, proposing new infrastructure as a vehicle to explore the ability of architecture to embody multiple narratives. By documenting built form, geology, hydrology, history, and mythology, the thesis illustrates the Hinnom/Rababa Valley as the space of the in-between, neither east nor west, bridging the urban hilltops with the underworld. The boundary partakes in both and neither sides simultaneously. Building on its multiplicity of meanings – of its ‘stories so far’ – the thesis attempts to re-imagine a new relationship to the ground.

The study aims to investigate an appropriate wastewater treatment process to treat domestic wastewater in Hanoi City which contain low-strength for COD (120-200 mg/L) but high in nitrogen content (10-40 mg/L). A lab scale anoxic-oxic system with a hollow fiber-Membrane Separation Bioreactor was operated at a flow rate of 5-10 L/h over a period of 150 days. The reactor was operated at different sludge recirculation rates. The MBR maintained relatively constant transmembrane pressure. During 150 days of reactor operation, treated water quality have COD of around 20 mg/L, NH4-N of less than 1 mg/L, NO3-N of less than 5 mg/L. The system shows good and stable efficiency for organic matter and nitrogen removal without adding an external carbon source and coagulants. The results based on the study indicated that the proposed process configuration has potential to treat the low-strength wastewater in Hanoi. / Mục tiêu của nghiên cứu là đề xuất được một công nghệ hiệu quả và phù hợp để xử lý nước thải sinh họat ở các đô thị của Việt nam, là loại nước thải được thu gom từ hệ thống thoát nước chung có nồng độ chất hữu cơ thấp (COD 120-200 mg/l) nhưng hàm lượng chất dinh dưỡng như Nitơ, Phốt pho khá cao (T-N: 10-40 mg/L). Chúng tôi đã nghiên cứu và vận hành chạy thử mô hình xử lý sinh học yếm khí - kỵ khí (AO) kết hợp với màng vi lọc ở quy mô mô hình phòng thí nghiệm (công suất 5-10 L/h) ở các chế độ công suất bùn tuần hoàn khác nhau. Kết quả xử lý trong thời gian 5 tháng vận hành mô hình cho thấy chất lượng nước thải sau xử lý có hàm lượng COD nhỏ hơn 20 mg/L, NH4-N nhỏ hơn 1 mg/L, NO3-N nhỏ hơn 5 mg/L. Hiệu suất xử lý chất hữu cơ và chất dinh dưỡng rất ổn định và hệ thống không phải sử dụng các nguồn bổ sung chất hữu cơ hay các hóa chất trợ lắng như các công nghệ đang áp dụng. Kết quả cho thấy công nghệ AO kết hợp màng vi lọc có khả năng áp dụng thực tế, phù hợp với những nơi có quỹ đất nhỏ, chất lượng nước sau xử lý rất cao có thể phục vụ cho mục đích tái sử dụng.

<p>Large amounts of human pharmaceutical products are consumed worldwide. Many drugs and their metabolites, referred to as pharmaceutically active compounds (PhACs), are not fully metabolized prior to household discharge resulting in their common occurrence in wastewater treatment plants (WWTPs). In most instances, WWTPs present the first treatment opportunity for removing PhACs and preventing significant environmental exposure. Because most municipal WWTPs rely on the microbial component of the activated sludge process, there is a need to estimate the influence of PhACs in wastewater influent on the activated sludge microbial communities and the treatment performance of WWTPs. The objective of this dissertation was to determine the impact of selected PhACs (i.e., ketoprofen, naproxen, clofibric acid, carbamazepine and gemfibrozil) on activated sludge microorganisms and key individual microbial species in domestic wastewater treatment. Analyses were performed in batch reactors initially and then in laboratory-scale sequencing batch reactors (SBR) which mimic WWTP operations. Ammonia oxidizing bacteria (AOB) were selected as indicator organisms because of their importance in wastewater treatment and demonstrated sensitiveness to toxic compounds. </p><p>The batch experiments results suggested that microbial growth inhibition was correlated to organic loadings. In the presence of 0.2% (v/v) ethanol, significant inhibition, ranging from 34 to 43%, was observed for all PhACs other than clofibric acid. </p><p>Nitrification inhibition studies using Nitrosomonas europaea, a model AOB strain showed that ketoprofen, naproxen, carbamazepine and gemfibrozil inhibited nitrite production. The corresponding maximum nitrification inhibition rates were 25, 29, 22 and 26%, respectively. Inhibition was shown to increase with PhAC concentration for concentrations greater than 0.1 µM. Results from membrane integrity tests suggest that the inhibition may be due to the disturbance of the cell membrane by PhACs and such inhibition was shown to be irreversible. </p><p>Even though PhACs were shown to inhibit the nitrification rate in pure culture studies, the performance of SBRs exposed to individual PhACs was not adversely affected neither in terms of COD nor ammonia removal. Microbial fingerprinting for both total bacteria and AOB confirmed that no significant shifts occurred when microbial communities were exposed to PhACs. However, some PhACs introduced in binary mixture were found to both inhibit the nitrification of N. europaea as well as the performance of SBRs. The mixture composed of 0.5 &#956;M ketoprofen and 0.5 &#956;M naproxen showed significant inhibition (25%) on the nitrite production of N. europaea although neither 0.5 &#956;M ketoprofen nor 0.5 &#956;M naproxen had significant effect when presented alone. Similarly, both COD and ammonia removal were significantly impacted by binary mixtures of PhACs. These results suggest that mixture effects can play an important role in an overall treatment's nitrification potential and this phenomenon should be further investigated.</p> / Dissertation

Most of wastewater treatment plants (WWTP) are operated under low loading both in water quality and water capacity (flow rate) in Taiwan. Because various treatment methods used in WWTP would cause different power consumptions. In general, the flow rate of wastewater treated is proportional to the power consumption. The purpose of this study is simulating water quality and water capacity with a case of municipal wastewater treatment plant, using standard activated sludge method. In this work we will investigate the feasibility of save power using operation and parameters adjustment in wastewater system. A further step is to conduct the save energy in current WWTP under normal wastewater treatment capacity and national effluent standard. Results showed the major save energy was at inflow pump and aeration system of biological treatment stage. Both power consumptions of two were about 60 ~70 % of total power consumption in the plant. Thus we should focus the operating conditions to plan the save energy project, and calculate the total power system and energy consumption of all unit facilities before we are going to improve the energy save in WWTP. Important note is firstly to select units and facilities having high energy consumption for evaluating the possibility of energy save. Secondly is develop and using a good management system to attain the goal of save energy.