Due to eutrophication of aquatic environment, massive growth of algae and cyanobacteria occurs and the seasonal algal bloom is formed. Drinking water treatment plants have to deal with the increased amount of cells as well as organic compounds produced by algae and cyanobacteria (so-called AOM). Moreover, the presence of AOM causes a reduction in the efficiency of coagulation, which is an essential process in drinking water treatment. To increase coagulation efficiency, supportive methods, such as ozone oxidation, are added usually prior to coagulation. While many studies focused on the ozonation of algal and cyanobacterial cells, little is known about the effect of ozonation on AOM. This diploma thesis focused on the evaluation of the effect of ozonation in combination with coagulation on the removal of cellular organic compounds (COM) produced by cyanobacteria Microcystis aeruginosa. The effect of ozonation before or after coagulation on COM removal was investigated. The degradation of microcystins, which are naturally contained in the COM sample, was also monitored. Various ozone doses (1 - 10 mg/L) were tested at three pH values - 5, 7 and 9. Two coagulants were utilized - aluminium sulphate and ferric sulphate. Ozonation removed COM negligibly. However, eliminated microcystins, the degradation...

This project investigated the bacteria in water entering and leaving the slow sand filters at Ringsjö Water Works using flow cytometry. The purpose was to explore the possibility of utilising flow cytometry as a monitoring method for optimising water production using slow sand filters. Data describing the bacterial community in water was collected over seven weeks and analysed with FlowJo, flow cytometric image comparison and Minitab. The total cell count, intact cell count and the percentage of high nucleic acid bacteria were analysed. These parameters were highly dependent on scraping events, water entering the filters and season. The results indicated that flow cytometry has great potential for use as a monitoring method, although more data should be collected to establish expected trends and secure baseline values for routine comparisons. / <p>Fördröjning av publikation fram till 31 december 2020.</p>

D. Tech (Department of Chemistry, Faculty of Applied and Computer Sciences) Vaal University of Technology. / Trivalent arsenic (As(III)) and hexavalent chromium (Cr(VI)) toxicity have necessitated a great deal of research into the remediation of contaminated water. The techniques applied including oxidation, coagulation-flocculation and ion exchange have suffered drawbacks due to the high cost of materials and equipment, complex operations and secondary pollution among others. Adsorption, however, remains a cost-effective solution in the remediation of contaminated water. The use of biosorbent materials further lowers the cost of the adsorption process and improves its eco-friendliness. These biomaterials, however, suffer some drawbacks as poor porosity, low adsorption capacities and mechanical strength thus require modifications to improve their applicability as biosorbents. In this work pine cone powder, a waste from pine trees, was used as a biosorbent for the removal of As(III) and Cr(VI) from water. The powder was pre-treated with Fenton’s reagent to oxidize some of the functional groups and provide more binding sites. Iron oxide magnetic nanoparticles (magnetite) were incorporated into the pine cone matrix to form a magnetic composite with higher heavy metal affinity. The magnetite nanoparticles were also doped with manganese to improve their redox capacities and aid in the oxidation of the toxic As(III) to the less toxic As(V) and allow for improved binding. The adsorbents used in the study were therefore named as Fenton’s treated pine cone powder (FTP), pine cone -magnetite composite (FTP-MNP), magnetite nanoparticles (MNP), manganese doped magnetite nanoparticles (Mn MNP) and manganese doped pine cone-magnetite composite (Mn FTP-MNP). The prepared materials were fully characterized, and the adsorption process was optimized for both As(III) and Cr(VI) removal from aqueous solution. After modification the surface area of the particles increased in the order Mn MNP>MNP>Mn FTP-MNP>FTP-MNP>FTP. Surface and Xray analysis confirmed the formation of magnetite by the presence of both ferric and ferrous ion states on the surface and characteristic diffraction peaks for magnetite. The adsorption data was fitted into isotherm and kinetic models and the nature of adsorption was determined from the thermodynamic and kinetic parameters. Equilibrium studies indicated that the adsorption followed Langmuir isotherm for all adsorbents and was thus monolayer in nature, further analysis indicated that chemisorption was the predominant type of adsorption with ion exchange being the predominant mechanism of adsorption. Spent adsorbents were tested for reusability and displayed excellent adsorption capacities when used for up to three times. Adsorption mechanism was evaluated using characterization techniques and the ion-exchange mechanism inferred from thermodynamic data was confirmed spectroscopically with redox reactions aiding in the removal of the pollutants from water. The introduction of competing anions in solution, lowered the adsorption efficiency of both arsenic and chromium on the adsorbent indicating that there was competition for adsorption sites.

<p>This dissertation investigates the factors which affect the removal of arsenic from groundwater by adsorption and coagulation technologies, including the interactions between As and natural organic matter (NOM). Humic acid (HA) was utilised as an NOM analogue, and was shown to be capable of both complexing and oxidising As, depending upon the prevailing conditions. The arsenic removing capabilities of three iron oxide coated sands (IOCS) were investigated, including IOCSW, a waste material from a local drinking water treatment plant generated during the removal of iron and manganese. IOCSW was highly effective at removing both As(V) and As(III) from synthetic water matrices (qmax = 78.3 &micro;g As(V)/g and 99.1 &micro;g As(III)/g). The negative effects of competitive anions (phosphates, silicates and HA) on arsenic removals were not significant enough to preclude the application of IOCSW for arsenic removal during drinking water treatment. The removals of both As and NOM by coagulation and enhanced coagulation with pH correction and preoxidation were also investigated. As(V) &nbsp;was more readily removed by coagulation than As(III), so that the most efficient coagulation treatment investigated for arsenic and NOM removal applied preozonation with subsequent combined coagulation with polyaluminium chloride and ferric chloride. Different groundwaters displayed large variations in the As and NOM removal behaviours. Response surface methodology (RSM) was therefore applied to investigate &nbsp;the interactions between As and NOM during ferric chloride coagulation and optimise their combined removals. Multiple interaction effects were observed during this investigation, highlighting the importance of utilizing RSM to optimise drinking water treatment technologies.</p> / <p>Ova disertacija ispituje faktore koji utiču na uklanjanje arsena iz podzemne vode primenom adsorpcija i koagulacije, uključujući i interakcije između arsena i prirodnih organskih materija (POM). Huminska kiselina (HA) je korisćena kao model za POM, a pokazano je da može i da kompleksira i da oksiduje As, u zavisnosti od eksperimentalnih uslova. Ispitivane su mogućnosti uklanjanja arsena za tri peska obložena gvožđe oksidom (IOCS), uključujući IOCSW, koji je dobijen sa postrojenja za tretman vode za piće i potiče iz procesa uklanjanja gvožđa i mangana. IOCSW se pokazao kao visoko efikasan za uklanjanje As(V) i As(III) iz sintetičkih vodenih matriksa (q_max = 78.3 &micro;g As(V)/g i 99.1 &micro;g As(III)/g). Negativni efekti kompetirajućih jona (fosfata, silikata i HA) na uklanjanje arsena nisu bili dovoljno značajni da bi se isključila primena IOCSW za uklanjanje arsena tokom tretmana vode za piće. Zajedničko uklanjanje As i POM koagulacijom i unapređenom koagulacijom uz pode&scaron;avanje pH i kombinovanje sa oksidacionim predtretmanima je takođe ispitivano. Bolje uklanjanje koagulacijom postignuto je za As(V) u odnosu na As(III), stoga se kao najefikasniji ispitivani koagulacioni tretman pokazalo uklanjanje arsena i POM primenom predozonizacije praćene kombinovanom koagulacijom sa polialuminijum hloridom i gvožđe hloridom. Ispitivanja na različitim podzemnim vodama, pokazala su velike varijacije u pona&scaron;anju As i POM tokom tretmana. Iz tog razloga je primenjena metodologija odzivne povr&scaron;ine (RSM) u cilju ispitivanja interakcija između As i POM tokom koagulacije gvožđe hloridom i optimizacije njihovog kombinovanog uklanjanja. Sagledavanje većeg broja interakcija primenom metodologije odzivne povr&scaron;ine potvrđuje važnost njegove primene pri optimizaciji tretmana vode za piće.</p>

Effective adsorbents for polyfluorinated compounds (PFCs) were successfully prepared. And they were tested in the adsorption of perfluorooctanoic and perfluorooctanesulfonic acids. Bridged silsesquioxanes containing secondary and tertiary amino groups were synthesized by sol-gel condensation of bis[3-(trimethoxysilyl)propyl]amine and bis[3-(methylamino)propyl]-trimethoxysilane in acidic media with surfactants. Obtained materials are mesoporous with a high BET surface area. They combine high structural stability with a high concentration of surface amino groups serving as adsorption sites. Batch adsorption tests demonstrated their extremely high adsorption capacity on PFCs: in some experiments, it reached up to 88% of the adsorbent weight. Adsorption of PFCs changed the surfaces of the adsorbent nanoparticles from hydrophilic to hydrophobic thus providing their agglomeration and floatability. Column tests showed fast adsorption of PFCs even at high concentrations and high flow rates. Obtained results can be used in the development of an effective filtration device for clean-up of water contaminated by PFCs.

Una parte importante del trabajo desarrollado en la presente tesis está basado en la puesta a punto y aplicación de la técnica de la microscopía electroquímica de barrido (SECM). Con esta técnica se han caracterizado electroquímicamente superficies sobre las que se han sintetizado una serie de materiales electroactivos desarrollados por nuestro grupo de investigación. Dichos materiales se sintetizan sobre diferentes substratos con el fin de disponer de electrodos de trabajo con aplicación en el contexto del tratamiento electroquímico de aguas residuales contaminadas con colorantes azoicos, provenientes de procesos de tintura en industrias textiles. Entre las superficies desarrolladas se incluyen: ¿ Ánodos dimensionalmente estables (DSAs) fabricados a partir de una superficie de Ti recubierta de SnO2 (Ti/SnO2), dopada con Sb (Ti/SnO2-Sb) y estabilizada con Pt (Ti/SnO2-Sb-Pt). ¿ Un tejido de poliéster (PES) recubierto de polipirrol (PPy) dopado con antraquinona sulfonato (PES/PPy-AQSA) o fosfotungstato (PES/PPy- PW12O403-). ¿ Un tejido de PES recubierto de polianilina (PANI) sintetizada en medios sulfúrico (PES/PANI-HSO4-) y clorhídrico (PES/PANI-Cl-). ¿ Un hilo de Pt recubierto de PANI con Pt electrodispersado (Pt/PANI-Pt). ¿ Un tejido de fibra de carbono recubierto de PANI (C/PANI) con o sin Pt electrodispersado (C/PANI-Pt). ¿ Un tejido de PES recubierto con óxido de grafeno (GO) o con su forma reducida (RGO). Los análisis locales efectuados a las superficies anteriormente descritas permitieron determinar su electroactividad frente a los pares redox Fe(CN)63-/4- y Ru(NH3)63+/2+ seleccionados como mediadores. Las curvas experimentales de aproximación obtenidas con el sistema en modo feedback, se compararon con las curvas teóricas establecidas por la teoría SECM para un substrato conductor (feedback +) y un substrato aislante (feedback -). Las imágenes SECM en 2D y 3D permitieron observar la distribución de la actividad electroquímica superficial para las diferentes muestras. Los resultados obtenidos con la microscopía SECM se utilizaron para validar los procedimientos de síntesis del material electroactivo en lo concerniente a su electroactividad y a la homogeneidad de su distribución. Las superficies textiles presentan una topografía muy irregular en comparación con la superficie metálica de un DSA. Aspecto especialmente reseñable en las muestras textiles es la influencia que ejerce la topografía del substrato textil en la imagen SECM de la electroactividad con el microelectrodo moviéndose a altura constante con respecto al substrato. En este sentido, las imágenes SECM obtenidas sobre las muestras textiles muestran como la electroactividad superficial reproduce el patrón geométrico del tejido. La influencia en la actividad electroquímica de aspectos tales como: tiempo de vida útil/corrosión en el caso de los DSAs, tipo de dopante/pH en el caso de la superficie PES/PPy, influencia del pH en las muestras de PES/PANI, el estado de oxidación de la especie electroactiva y la influencia del mediador (par redox) en el caso del grafeno, ha quedado puesta de manifiesto claramente en los estudios efectuados con la microscopía SECM. Una segunda parte importante del trabajo realizado en la presente tesis, se desarrolla como continuación a los trabajos que el grupo de investigación viene realizando dentro del contexto del tratamiento electroquímico de colorantes azoicos en disolución acuosa. Así, en el capítulo 2 de la presente tesis, se estudia el desarrollo, caracterización y aplicación de una serie de electrodos fabricados a partir de un tejido activo de fibra de carbono. El objetivo que persigue el desarrollo de estos electrodos está en su aplicación a procesos industriales tales como: la electrooxidación de moléculas relativamente sencillas como por ejemplo metanol o, de acuerdo con nuestra línea de investigación, para el tratamiento electroquímico de aguas contaminadas con colorantes azoicos provenientes de los procesos de tintura en industrias textiles. Entre los electrodos textiles de fibra de carbono desarrollados en el capítulo 2 de la presente tesis se incluyen: ¿ Electrodos textiles de carbono sin modificar. ¿ Electrodos textiles de carbono modificados con Pt disperso. ¿ Electrodos textiles de carbono recubiertos de PPy o PANI. ¿ Electrodos textiles de carbono recubiertos de PPy o PANI con Pt disperso. Dos tipos de geometrías se eligieron a la hora de fabricar los electrodos de fibra de carbono anteriormente citados. Los electrodos monodimensionales (WE1D) fueron preparados a partir de una hebra tomada del propio tejido. Los electrodos bidimensionales (WE2D) se prepararon a partir de una banda de (1 cm x 3 cm) cortada del tejido de carbono. Por medio de la voltametría cíclica (CV) y utilizando los WE1D se establecieron las condiciones de síntesis para la fabricación de los WE2D modificados. Además, por medio de la CV se estudió la respuesta electroquímica de los WE1Ds en diferentes sistemas electroquímicos tales como: una disolución de H2SO4, una disolución de CH3OH/H2SO4 y una disolución de amarante/H2SO4. Para este último sistema, además, se utilizó un electrodo de carbono vítreo (GCE) ya que proporcionaba una respuesta voltamétrica más precisa que la obtenida con los WE1Ds. En la caracterización electroquímica que se realizó a los electrodos WE2D, la microscopía SECM jugó un papel relevante. Con la configuración 2D no era posible obtener voltagramas precisos que nos permitieran observar el comportamiento electroquímico de los diferentes WE2D modificados. Con la microscopía SECM, sí se pudo medir la actividad electrocatalítica de las diferentes superficies validándose, entonces, las condiciones de síntesis utilizadas. Algunas de estas condiciones, como los rangos de potencial, se habían establecido previamente para los WE1D. Así, la microscopía SECM se muestra como alternativa a la CV para la medida de la electroactividad superficial y de la distribución del material electrocatalítico para este tipo de muestras. Además de la caracterización electroquímica, se realizó también una caracterización morfológica de las superficies electródicas mediante la toma de imágenes por medio de la microscopía electrónica de barrido (SEM) y del microscopio estereoscópico. El estudio voltamétrico efectuado para el sistema amarante/H2SO4 con los electrodos textiles WE1D y el electrodo GCE permitió el establecimiento de los potenciales de trabajo a los que realizar la electrólisis de oxidación y de reducción a potencial controlado con los electrodos WE2D, WE2D/Pt y WE2D/PANI-Pt. Con los electrodos de trabajo anteriores, se llevan a cabo diferentes electrólisis de electroreducción y electrooxidación a una disolución de amarante en medio sulfúrico utilizando una célula en forma de ¿H¿ con separación de compartimentos. El seguimiento del proceso de degradación de la molécula de amarante y por ende de la decoloración de la disolución, se efectuó por medio de la cromatografía líquida de alta resolución (HPLC) y las espectroscopías UV-visible, fluorescencia de emisión e infrarroja por transformada de Fourier con reflexión total atenuada (FTIR-ATR). Los resultados de eficiencia obtenidos en las electrólisis confirman la elección de los potenciales de trabajo seleccionados. El porcentaje de decoloración tanto con las electroreducciones como con las electrooxidaciones se sitúa por encima del 90 %. También se comprobó que la presencia de platino trae consigo una significativa reducción del tiempo de electrólisis para la electrooxidación a 900 mV. Los análisis de los espectros UV, de fluorescencia de emisión y FTIR-ATR permitieron establecer diferencias significativas en relación con el tipo de proceso electroquímico (electroreducción/electrooxidación), tipo de electrodo (modificado/no modificado) y la presencia/ausencia de cloruros en el medio de reacción. Con este trabajo se establece una metodología de cara a futuros estudios con otros colorantes azoicos utilizando electrodos basados en el tejido de fibra de carbono. / Fernández Sáez, J. (2014). Análisis por microscopía electroquímica de barrido de superficies electroactivas y desarrollo-caracterización de electrodos basados en un tejido de fibra de carbono [Tesis doctoral]. Editorial Universitat Politècnica de València. https://doi.org/10.4995/Thesis/10251/38239 / Alfresco

Phosphorous and nitrogen are vital elements for the well-being of biological life. Industrial discharges, waste water infiltration systems, conventional waste water collection and treatment systems, agricultural runoffs and landfill leachates had been emitting significant quantity of these nutrients into water bodies. These induced negative consequences to the environment including eutrophication of aquatic water bodies, toxicity to marine life and depletion of phosphate resources. Reactive filter technology is developed based on the need to remove and retain nutrients from waste water while improving the quality of effluents from emission sources. Reactive filter materials are used to build filter bed systems that treats domestic waste water, storm water, landfill leachates and contaminated subsurface water to the desired quality. In the past natural minerals such as zeolites and industrially produced polonite had been subject to laboratory study for the sorption of ammonium, heavy metals and phosphorous. The following paper is based on the results of experiment consisting of two columns packed with mordenite and polonite reactive materials filtering in series to reduce NH4 and PO4 content of a waste water. Septic tank effluent pre filtered using 0.45 μm filter is used as influent waste water into the dual columns. The dual column filtered a total of 24.07l s (372PV) and 23.42 ls (496PV) of the waste water. Sampling of the feed water and filtrates of both columns were done every second day with measurement of pH, conductivity and temperature. Analyzed samples confirmed that the dual column filtration resulted in re-moval efficiency of 84.39 % (PO4), 67.98 % (NH4) and -37.762.8 % (NOx). Filtration in the first (mordenite) column resulted in relatively larger proportion of the influent ammonium ion exchange than sorption of phosphate while the filtration in the second (polonite) column sorbed quite high amount of phosphorous than ammonium from effluent of the first column. Saturation of mordenite occurred faster even though there was sorption potential for few more of influent ammonium. All PO4 removal in mordenite column occurred above breakthrough condition. Polonite packed column was in a condition of a third of it’s saturation potential for PO4 removal at the end of the experiment. pH of samples was the parameter which is correlated significantly with filtration in polonite column than temperature and electrical conductivity. The performance of polonite was higher at higher pH than at lower pH. The mean concentrations of the dual column effluent were 0.77 mg-PO4/l and 11.13 mg-NH4/l. This is acceptable by the standards of environmental laws. The result of the experiment is valuable in prediction of performance and designing of real time filter bed.

Advanced oxidation technology (AOT) has been used to destroy microorganisms in ballast water by breaking down the cell membranes. The primary objective of this study was to determine the effects of a ballast water treatment system that uses a combination of UV-C (λ=254 nm), Vacuum-UV (VUV; λ=185 nm) and photocatalytic titanium dioxide (TiO2) on a freshwater algae, Pseudokirchneriella subcapitata, and a marine algae, Tetraselmis suecica. The coupling of a semiconductor, such as TiO2, with a UV source is known as an advanced oxidative technology (AOT). To test the effects of TiO2 and wave length on algae, dose-response experiments were conducted to determine the species median lethal dose (LC50) for each of the following treatments: UV-light emitted at 254 nm (UVλ=254 nm), UV-light emitted at 254 nm in the presence of TiO2 (AOTλ=254 nm), and UV-light emitted at λ=254 nm (90 %) and 185 nm (90 %) in the presence of TiO2 (AOTλ=185 + 254 nm). In both species, TiO2 significantly increased mortality, most likely due to the biologically harmful radicals generated at the TiO2 surface. The addition of the 185 nm wavelength significantly increased cell mortality in P. subcapitata, but not in T. suecica. Across all three treatments, P. subcapitata was more sensitive than T. suecica. The secondary purpose of this study was to assess the applicability of ImageJ, an image analysis software, for highthroughput data to analyze the effectiveness of ballast water treatment. ImageJ has been used to rapidly and accurately perform cell Live/Dead analysis; however, several hurdles were identified.

Municipal wastewater contains a significant amount of nutrients such as phosphorus (P) and nitrogen (N). Therefore have the interest of recovering these nutrients at wastewater treatment plants (WWTP) increased. Nutrient recovery would generate revenue for the WWTP, as it is possible to sell the products as fertiliser. Today, there are several techniques on the market to recover P as magnesium ammonium phosphate (MAP) and N as ammonium sulphate (AMS). Urine is the fraction contributing with the highest concentration of nutrients. Techniques to separate urine from the rest of the wastewater have been developed. These techniques enable the possibility to recover nutrients from the urine fraction separately; this is beneficial since the nutrient concentration would be higher. The purpose with this study was to examine the possibility for increased nutrient recovery at centralised WWTPs through urine separation.   Different techniques for nutrient recovery were compared by their recovery efficiency, chemical demand, and hydraulic retention time (HRT). A WWTP with enhanced biological P removal was modelled with Danish Hydraulic Institute’s (DHI) software WEST. Eight scenarios, with different percentage of the population equivalents using urine separation techniques, were simulated. The P recovery was calculated from phosphate (PO4) in the hydrolysed excess sludge and the separated urine. The N recovery was calculated from the ammonium (NH4) in the supernatant from the anaerobe digester. The theoretical biogas production was also calculated, from the modelled sludge.    The comparison of P recovery techniques showed no substantial differences in their recovery efficiency, chemical demand, and HRT. The comparison of N recovery techniques showed three techniques with a higher efficiency than the other methods. Ekobalans Fenix AB, CMI Europe Environment, and Organics developed these techniques. To determine which method to use, requests for proposal from different providers are recommended. As the urine separation increased, the influent P and N load decreased. When the urine separation increased and the operational parameters were kept constant, the effluent concentration of P and N decreased. The ratio of total Kjeldahl nitrogen (TKN) and total nitrogen (TN) however increased as the urine separation increased. The total MAP production calculated from the modelled hydrolysis showed that the production increased as the urine separation increased. On the other hand, the total MAP production from calculated hydrolysis showed a decrease in production as the urine separation increased. The difference in these results could be because of the performance of the modelled hydrolysis was better with a smaller nutrient load, resulting in a larger release of PO4 as the urine separation increased. The total AMS production increased as the urine separation increased. This, due to the increase of the TKN:TN ratio. The biogas production was not substantially affected by the increased urine separation.

Die Behandlung von Regenwassereinleitungen aus Misch- und Trennsyste-men in Gewässer stellt eine der entscheidenden Kriterien für die Erreichung der Zielstellung der guten Gewässerqualität nach der EU-Wasserrahmen-richtlinie dar. Für die Begrenzung und Behandlung von Mischwassereinleitungen stehen eine Vielzahl von Richtlinien und Gesetzen sowie Arbeits- und Merkblätter der DWA zur Verfügung. Diese sind emissions- und immissionsbasiert, fokussieren aber hauptsächlich auf Möglichkeiten der Behandlung im Kanalnetz. Mit dem DWA-Themenband 'Technische Maßnahmen zur Behandlung von erhöhten Mischwasserabflüssen in der Kläranlage' werden hinsichtlich einer integrierten Betrachtung erstmalig Maßnahmen in der Kläranlage zusammenfassend erläu-tert. Ein Verfahren zur Mischwasserbehandlung in der Kläranlage stellt dabei das Bypassverfahren dar. Mit diesem ist eine Mehrbehandlung von Mischwasser unter Ausnutzung der vorhandenen Reserven der Kläranlagen zur Verringe-rung der Gewässerbelastung bzw. zur Substitution von Speichervolumen im Kanalnetz möglich. Weiterhin kann mit dem Verfahren eine Stabilisierung der Funktionstüchtigkeit des Nachklärbeckens bei bevorstehendem Schlammab-trieb ermöglicht werden. Im Rahmen der Arbeit werden detailliert die Grundlagen und die durchgeführten Versuche im labor-, halb- und großtechnischen Maßstab sowie die erreichten Ergebnisse dargestellt. Mit Hilfe der dynamischen Simulation werden die statt-findenden Prozesse beschrieben, die Eliminationsgrade ermittelt und allge-meingültig aufbereitet. Es ergeben sich Eliminationsgrade des zusätzlich be-handelten Mischwassers von ca. 60 % für CSB und ca. 50 % für TKN sowie ein funktionaler Zusammenhang über das Rückführungsverhältnis. Ausgehend von der hydraulischen Reserve der Nachklärbecken wird eine Be-messungsrichtlinie für die Volumenstrombemessung des Bypass erarbeitet und die damit verbundenen Auswirkungen auf das Nachklärbecken beschrieben. Bei Einhaltung der derzeit geltenden Bemessungsparameter für Nachklärbe-cken ist durch das Bypassverfahren mit einer deutlichen Entlastungsfrachtredu-zierung zu rechnen und dabei werden die Überwachungswerte der Anlage ein-gehalten. Die Reduzierung der Entlastungsfracht kann über die Bewertung der Gesamtemission mit Beckenvolumina im Kanalnetz verglichen werden und da-mit eine Substitution von Speichervolumen generieren.