Os compostos (coloidais, suspensos e solúveis) presentes na água residual possuem diferentes características físico-químicas e diferentes massas moleculares. Pesquisadores têm se dedicado ao entendimento mais específico da parte solúvel do efluente. O fracionamento das substâncias orgânicas em diferentes classes e diferentes tamanhos é um dos métodos utilizados para a caracterização dos compostos orgânicos da água residual. Acredita-se que este método possa detectar as alterações nos valores residuais dos compostos orgânicos de forma mais precisa que os métodos tradicionais, i.e. DBO e DQO. Sendo assim, e sabendo do crescente uso dos projetos de pós-tratamento dos efluentes de ETE e reúso destes, fica a clara a avaliação da eficiência dos processos de pós-tratamento e a importância da quantificação e caracterização da matéria orgânica residual no efluente pós-tratado. Os objetivos deste projeto de pesquisa foram avaliar a remoção da carga orgânica residual no efluente do tratamento biológico do processo de lodo ativado da ETE Jesus Netto, utilizando diferentes parâmetros de coagulação/floculação utilizando cloreto férrico, sulfato de alumínio e cloreto de polialumínio como coagulantes, e análise de carbono orgânico dissolvido juntamente com a técnica de distribuição da massa molecular para avaliar essa remoção. As análises mostraram uma redução dos compostos orgânicos presentes no efluente secundário, em termos de carbono orgânico dissolvido, da ordem de 45% para o cloreto férrico e 38% para os sais de alumínio. A distribuição da massa molecular também sofreu alterações, notando-se o aumento dos compostos de menor massa molecular e a redução dos compostos de maior massa molecular. Os resultados corroboram com outros estudos realizados com efluentes secundários e águas de abastecimento sobre o impacto dos processos físico-químicos na distribuição da massa molecular. / The compounds (colloidal, suspended and soluble) present in the waste water have different physicochemical characteristics and different molecular masses. Researchers have dedicated themselves to the more specific understanding of the soluble part of the effluent. The fractionation of the organic substances in different classes and different sizes is a method widely used for the characterization of the organic compounds of the residual water. It´s believed that this method can detect changes of organic compounds residual values more accurately than traditional methods, i.e. biological oxygen demand and chemical oxygen demand. Therefore, knowing the increasing use of WWTP effluent after post-treatment processes and their reuse, it is clear that the evaluation of the post-treatment efficiency and the importance of the quantification and characterization of the residual organic matter in the post-treated effluent. The objectives of this research project were to evaluate the removal of the residual organic matter in the effluent from the biological treatment of the activated sludge process of the Jesus Netto WWTP using different coagulation/flocculation parameters with ferric chloride, aluminium sulfate and polyaluminum chloride (PAC) as coagulants, and dissolved organic carbon and molecular mass distribution analyses to evaluate the organic matter removal. The analyzes showed a reduction of the organic matter present in the secondary effluent, in terms of dissolved organic carbon, up to 45% for ferric chloride and 38% for aluminum salts. The distribution of the molecular mass also changed, with the increase of the compounds of lower molecular mass and the reduction of the compounds of higher molecular mass. The results corroborate with other studies carried out with secondary effluents and water supply on the impact of physicochemical processes on the molecular weight distribution.

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...

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Many different stormwater control measures (SCMs) can be implemented in order to mitigate issues with polluted stormwater flows into receiving water bodies.  The treatment function of  SCMs is commonly based on the removal of particles by sedimentation, thereby also removing pollutants associated with particles. In recent years, more attention has been given to characterizing and understanding of different particle size fractions and their association with pollutants commonly found in stormwater. It has become increasingly clear that the smaller sized particles are very important pollutant transporters and should be considered when designing and implementing SCMs. However, the settling velocities for smaller sized particles are very low and may not be effectively removed in existing SCMs. One treatment process with a proven ability to enhance sedimentation is coagulation/flocculation, widespread in water and wastewater treatment, but with very few accounts of it being used in a stormwater context. This thesis aims to investigate the treatability of stormwater with a coagulation/flocculation process. This includes the determination of operating conditions, the dominating coagulation mechanism and the reduction efficiency of stormwater related pollutants. The objectives of the thesis were achieved in laboratory tests treating stormwater in a jar-testing procedure. An initial screening of primary coagulants and flocculant aids was conducted using an urban snowmelt mixture. Five of the chemicals were then selected for an extended testing regime which was setup up to determine the operating conditions where maximal turbidity reduction was attained by measuring the pH, conductivity, alkalinity and zeta-potential over the tested doses for each coagulant. Criteria used for chemical selection included high turbidity reduction, low dose requirement and low pH/alkalinity impacts. Charge reversal was observed at positive zeta-potential indicating that the dominating coagulation mechanism was charge neutralization. The content of turbidity/total suspended solids, total organic carbon, total metals and hydrocarbons by >90%. Dissolved copper was reduced by 40% on average, and the reduction rates for dissolved zinc were varying with up to a 300% increase, presumably due to changes in pH, leading to a higher mobility. Changes in the particle size distribution after coagulation/flocculation as compared to sedimentation indicated an effect on the size fraction corresponding to smaller particles. The performance of the coagulation/flocculation process was also tested on road runoff collected from a central road in Luleå with a high traffic intensity. Two coagulants were tested, iron chloride and pre-hydrolyzed aluminum chloride. Reduction rates for the total metal fraction were >90% on average for both coagulants, but for the dissolved metal fractions differences could be observed between the coagulants with the iron chloride resulting in higher reductions for dissolved chrome (57% compared to 34%) and copper (47% compared to 30%). Both products increased the dissolved fractions of nickel and zinc due to lower final pH.

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Kommunalförbundet Norrvatten är en av Sveriges största producenter av dricksvatten och förser över 50 miljoner vatten till över 700 000 invånare i norra Stockholm. Vattnet är renat i Görvälnverket som har sedan år 2016 planlagt en expansion av verkets kapacitet och kvalité. Ett fokusområde för att förbättra reningsprocessen är implementering av membranteknik. I det här projektet har experiment utförts som ett fortsatt arbete av att integrera ultrafiltration med koagulering på en mikropilot. Syftet med projektet är att optimera driftparameterar (koaguleringsdos, pH och alkalitet, uppehållstid och omblandning) för processen och jämföra pilotens effektivitet för två typer av matarvatten (kol- och sandfiltrat). En lägre koaguleringsdos på 2.5 mg Al/L resulterade i en 18.9 % avskiljning av TOC och 21.3% minskning i UV254. I jämförelse med en högre dos på 3.8 mg Al/L, var effektiviteten 2 % bättre för TOC och 3 % bättre för UV254. Till följd av en låg ökning i effektivitet för en högre koagulantdos påvisar en lägre dosering ett bättre alternativ. Dessutom är det rekommenderat att vid uppskalandet av piloten mer försök genomförs för att få mer pålitliga data och att automatisk dosering implementeras eftersom dosering av koagulant var en svårkontrollerad parameter.pH inom intervallet 6.8 till 7.2 visade vara mest optimal för att minimera mängden aluminiumrester i permeatet. Experimenten på pH konstaterar att flockning är pH beroende och optimalt vid pH 7. Effektiviteten var också beroende av alkaliteten. Där bäst alkalinitet anpassades till mellan 40 och 50 mg HCO3/L, med högre än 50 mg HCO3/L minskade effektiviteten av avskiljningen, vilket tyder på sämre flockning vid basiska förhållanden. Karbonatdosering av 5 mL 0.01 M Na2CO3 /L obehandlat vatten uppnådde önskad alkalinitet och minimerade aluminiumrester i permeatet.  Uppehållstiden och konfigurationen av blandning indikerade ingen optimal justering. Emellertid, en jämförelse av försök med uppehållstiden och försök utan koaguleringdos visade dramatisk minskning i effektivitet till endast 2 % TOC avskiljning och 6 % UV254 minskning. Placering av ultrafiltrationsenheten efter kolfiltret jämfört med efter sandfiltret visade inga tecken på nedsatt effektivitet. Transmembrantrycket över membranet ökade över den experimenterade perioden från 0.02 till 0.06 bar och fluktuerade under drift mellan det första och sista försöket. Det var däremot ingen skillnad i trycket mellan kolfilter och sandfilter, vilket styrker beslutet att placera ultrafiltrationsenheten efter kolfiltret. / The municipal association Norrvatten is one of Sweden's largest drinking water producers and distributes over 50 million m3 of drinking water to around 700 000 inhabitants in northern Stockholm. The water is treated in the Görväln plant, which has since 2016 planned to expand its capacity and improve its water quality. One researched area for improving the treatment process is implementing membrane technology. In this project, experiments are performed as a continued work of integrating ultrafiltration with coagulation on a bench-scale plant. The purpose is to optimise the operating parameters (coagulant dosage, pH & alkalinity, retention time, and mixing) and compare the ultrafiltration removal efficiency for two types of feed water (carbon and sand filtrate).  A lower coagulant dosage of 2.5 mg Al/L resulted in removal efficiencies on average of 18.9 % TOC removal and 21.3 % UV254 reduction. Compared to the higher dosage of 3.8 mg Al/L, the removal efficiency was only decreased with 2 % TOC and 3 % UV254. Therefore, a lower dosage is a more suitable option. Although, more data needs to be collected for a more reliable optimal dosage. In addition, for the up-scaling of the pilot, automatic dosage control needs to be implemented as the coagulant dosage is difficult to control as a parameter. pH showed the best removal efficiency in the range of 6.8 to 7.2 and minimised aluminium residue in the permeate. It verifies that flock formation is pH-dependent and optimal close to 7. The efficiency also depended on the alkalinity, with the optimal alkalinity between 40 to 50 mg HCO3/L. Higher alkalinity decreased the efficiency, which supports the theory that too basic water hinders flock formation. With minimum dosage of 5 mL 0.01 M Na2CO3/L untreated water, the required alkalinity could be achieved without affecting the amount of aluminium in the permeate residue.  The retention time and mixing configuration did not result in an optimum adjustment. However, with no retention time at a coagulant dosage of 0 mg Al/mL, the efficiency was reduced drastically to 2 % TOC removal and 6 % UV254 reduction. The placement after the carbon filter showed no adverse signs on the removal efficiency compared with placing it after the sand filter. The TMP of the membrane increased over time from 0.02 to 0.06 bar, and higher fluctuations in TMP were noted in the last experiment compared to the first. The differences were identical for both carbon and sand filtrate, strengthening the decision to place the ultrafiltration unit after the carbon filter.

Microalgae are considered as a potential feedstock for many promising applications. Some active substances in microalgae have plant biostimulation effects potentially useful in agriculture. However, to produce such a microalgal biomass, specific microalgae cultivation and post-treatment processes must be designed to preserve active substances. A particular focus is provided on cultivation (tubular photobioreactor) and different plausible post-treatment scenarios for microalgae separation (flocculation and centrifugation) and preservation (sterilization and drying). For each step, yield and energy consumption are modeled using data taken from literature or lab and pilot scale experiments. Industrial equipment for scale-up process is also studied by comparing existing systems. These models enable to make an economic evaluation of the whole process and to study its profitability for each scenario. The breakeven price is calculated as a function of the production rate. Several parameters are suggested to improve system efficiency and profitability at the end of this study. However, a better microalgae characterization and more experiments on potential post-treatment systems are required to improve the accuracy of the model.

Water quality and space constraints have become major concerns regarding the No. 7 waste water dam at Petra Diamonds’ Cullinan mine. The unique location of the dam constrains further development, while unsustainable accumulation of waste water inside the dam increases the risk of potential environmental contamination from seepages and spillages. The dam retains a significant amount of very poor quality water. Its excessively high pH, dissolved salt content, density and extreme turbidity result from the concentration of natural weathering products of the diamond bearing kimberlite ore. The turbidity results from the dispersion of colloidal chlorite, saponite and nontronite clay. Along with the chemistry of the solution, their colloidal shape contributes equally significantly to the non-settlement of these suspended clays. Flocculation of the dispersed clay particles will provide (a) for easy and effective separation of the clay material from the waste water and (b) more convenient options for water treatment (and subsequent redistribution) This study was aimed at contributing to a better understanding of the dynamic interactions in the No 7 Dam system to contribute towards identifying a suitable means/method for chemical flocculation of the clay particles. The individual components of the system (clays, water quality) and influx contributors (kimberlite and its leachate) were systematically characterized by means of X-Ray Diffraction, X-Ray Fluorescence, petrographic microscopy, electron microscopy, electrophoretic mobility and standard water- and soil quality analyses. The baseline quality of the Cullinan kimberlite leachate was obtained based on ASTM D5744 principles. It was found that adjusting the pH-level and ionic strength of the waste water to the critical coagulation point (cK) (as determined by electrophoretic mobility and batch jar experiments) automatically induced coagulation. Higher valence cations were displaced from pH dependent surface charge sites by proton adsorption. The resultant increased ionic strength, in combination with decreased thickness of the ionic double layer, was sufficient for the automatic initiation of high strength disordered face-face and edge-face bonds. During batch Jar tests, flocculation initiated within 4 minutes after the addition of HCl (0.5 M) and total sedimentation completed within 3 hours. The use of commercial flocculants might decrease the sedimentation time. As expected a significant increase in dissolved salt content of the clear supernatant was observed. No re-dispersion of the dried clay occurred. Throughout the study geochemical modeling was performed with PHREEQC software to identify/determine possible effective experimental conditions, minimizing experimental time and expenses. The program was also used to model outcomes of the possible water treatment options, indicated in literature as viable options for similar situations. These options can be tested to extend upon the current research. / MSc (Environmental Sciences), North-West University, Potchefstroom Campus, 2015

Water quality and space constraints have become major concerns regarding the No. 7 waste water dam at Petra Diamonds’ Cullinan mine. The unique location of the dam constrains further development, while unsustainable accumulation of waste water inside the dam increases the risk of potential environmental contamination from seepages and spillages. The dam retains a significant amount of very poor quality water. Its excessively high pH, dissolved salt content, density and extreme turbidity result from the concentration of natural weathering products of the diamond bearing kimberlite ore. The turbidity results from the dispersion of colloidal chlorite, saponite and nontronite clay. Along with the chemistry of the solution, their colloidal shape contributes equally significantly to the non-settlement of these suspended clays. Flocculation of the dispersed clay particles will provide (a) for easy and effective separation of the clay material from the waste water and (b) more convenient options for water treatment (and subsequent redistribution) This study was aimed at contributing to a better understanding of the dynamic interactions in the No 7 Dam system to contribute towards identifying a suitable means/method for chemical flocculation of the clay particles. The individual components of the system (clays, water quality) and influx contributors (kimberlite and its leachate) were systematically characterized by means of X-Ray Diffraction, X-Ray Fluorescence, petrographic microscopy, electron microscopy, electrophoretic mobility and standard water- and soil quality analyses. The baseline quality of the Cullinan kimberlite leachate was obtained based on ASTM D5744 principles. It was found that adjusting the pH-level and ionic strength of the waste water to the critical coagulation point (cK) (as determined by electrophoretic mobility and batch jar experiments) automatically induced coagulation. Higher valence cations were displaced from pH dependent surface charge sites by proton adsorption. The resultant increased ionic strength, in combination with decreased thickness of the ionic double layer, was sufficient for the automatic initiation of high strength disordered face-face and edge-face bonds. During batch Jar tests, flocculation initiated within 4 minutes after the addition of HCl (0.5 M) and total sedimentation completed within 3 hours. The use of commercial flocculants might decrease the sedimentation time. As expected a significant increase in dissolved salt content of the clear supernatant was observed. No re-dispersion of the dried clay occurred. Throughout the study geochemical modeling was performed with PHREEQC software to identify/determine possible effective experimental conditions, minimizing experimental time and expenses. The program was also used to model outcomes of the possible water treatment options, indicated in literature as viable options for similar situations. These options can be tested to extend upon the current research. / MSc (Environmental Sciences), North-West University, Potchefstroom Campus, 2015