The increasing amount of microplastics found in the environment have underscored the urgency to identify, develop and deploy scenarios in which municipal wastewater treatment plants (MWWTPs) limit the release of urban microplastics into the environment. Simultaneously, the global trend towards a circular economy has defined the conditions for these scenarios in relation to the water-energy- nutrient nexus. This study has created a novel framework between studies into treatment technologies for microplastics removal in wastewater streams and circular economic objectives from policymakers with regard to the water-energy-nutrient nexus. The results of this study build on the existing evidence that MWWTPs release significant amounts of microplastics to both terrestrial and aquatic environments. This study has demonstrated how Multi-criteria Analysis (MCA) can be applied to analyse wastewater treatment scenarios for their ability to limit microplastic pollution from MWWTPs, whilst taking the water-energy- nutrient nexus into account. The MCA has identified MBR inci-eco as the best performing circular economic scenario for limiting microplastic pollution from MWWTPs in to be constructed plants. This scenario includes a Membrane Bioreactor (MBR) with Anaerobic Digestion, energy recovery through incineration and Phosphorus recovery through Ecophos. If already existing MWWTPs aim to upgrade their facility to limit microplastic pollution, CASPACUF with Pyreg as an energy-nutrient recovery is seen as the best performing scenario. The powder activated carbon with ultra filtration (PAC-UF) system would then be installed as an additional polishing step to an existing conventional activated sludge (CAS) system, significantly reducing upfront investment costs. Academia can build upon these results to initiate additional research into novel microplastic filtration specific technologies, business model innovation for wastewater treatment and microplastic pollution prevention at the source and in stormwaters. National and international policymakers should ban the distribution and sale of biosolids for direct land application to limit the pollution of microplastics from bio-solids. Furthermore, efforts should be put in place to limit microplastic pollution at the source by stimulating policies for a ban on the use of microbeads, limit tyre wear and improving design for e.q. washing machines. / Den ökande mängden mikroplast som finns i miljön har understrukit brådskan i att identifiera, utveckla och tillämpa strategier där kommunala avloppsreningsverk (MWWTP) begränsar utsläpp av urbana mikroplaster. Samtidigt har den globala trenden mot en cirkulär ekonomi definierat villkoren för dessa scenarier i förhållande till vatten-energi-näring-näxan. Denna studie har tagit fram ett nytt ramverk mellan studier om reningsteknologier för avlägsnande av mikroplast i avloppsvattenströmmar och cirkulära ekonomiska mål från beslutsfattare med avseende på water-energy-nutrient nexus. Resultaten av denna studie bygger på befintliga bevis på att kommunala avloppsreningsverk släpper ut betydande mängder mikroplast i både mark- och vattenmiljöer. Denna studie har visat hur Multi-Criteria Analysis (MCA) kan användas för att analysera avloppsreningsscenarier utifrån deras förmåga att begränsa mikroplastföroreningar från reningsverk, samtidigt som man tar hänsyn till vatten-energi-näring-näxan. MCA har identifierat MBR-inci-eco som det bäst presterande cirkulära ekonomiska scenariot för att begränsa mikroplastföroreningar från nya verk. Detta scenario inkluderar en Membrane Bioreactor (MBR) med anaerobisk nebrytning, energiåtervinning genom förbränning och fosforåtervinning genom Ecophos. Om redan befintliga verk ska uppgradera sin anläggning för att begränsa mikroplastföroreningar, ses CASPACUF med Pyreg som energi-näringsåtervinning som det bästa scenariot. Det pulveraktiverade kolet med ultrafiltreringssystemet (PAC-UF) skulle sedan installeras som ett ytterligare poleringssteg till ett befintligt konventionellt system för aktiverat slam (CAS), vilket avsevärt minskar investeringskostnaderna. Framtida forskning kan använda dessa resultat för att undersöka nya mikroplastfiltreringsspecifika tekniker, affärsmodellinnovation för avloppsrening och förebyggande av mikroplastförorening vid källan och i stormvatten. Nationella och internationella beslutsfattare bör förbjuda distribution och försäljning av biosolids för direkt markanvändning för att begränsa mikroplastföroreningar från biosolids. Vidare bör åtgärder vidtas för att begränsa mikroplastföroreningar vid källan genom att stimulera policyer för ett förbud mot användning av mikrokulor, begränsa däckslitage och förbättra designen för e.q. tvättmaskiner.

Pulp and paper mills are one of the top consumers of water related to industrial manufacturing, which ultimately leads to a large volume of heavily contaminated wastewater. This discharged effluent can have a harmful effect on the receiving aquatic environment and cause further ramifications downstream. Thus, a technically feasible and cost effective treatment solution for safe release from the mill is essential. Dissolved air flotation (DAF) has many applications and involves the formation of air microbubbles triggered by a drop to atmospheric pressure. When introduced into the wastewater, these microbubbles attach to the floc particles present and float to the surface. Another water treatment technology is ozone, a powerful oxidant, and has been widely used in water and wastewater treatment over recent decades, including color reduction in pulp and paper mill wastewater treatment. This thesis studied the effect pre-ozonation has on the DAF process in treating pulp and paper mill secondary effluent. Wastewaters from three mills with different initial water quality parameters were used, especially chemical oxygen demand (COD), turbidity, and color. The most suitable coagulant and coagulant aid, aluminum chlorohydrate and cationic polymer NS 4700P respectively, were selected, and an effective bench-scale experimental procedure was established. Pre-ozonation did not reduce the need for coagulant due to little change in the overall COD, color, or turbidity removal. However, ozonation did reduce color before coagulation, and the ultimate target removal of COD to 90 ppm was met with the conditions chosen. / Environmental Engineering

Urbanization affects in-stream biogeochemical processes that control nutrient export. Attempts to restore urban streams will not be successful unless the biological and physical controls on water quality are thoroughly understood. The objective of this study was to identify the relative influences of tributary dilution, groundwater discharge, and biological processing on nitrate concentrations in an urban stream during high and low flow periods. A wastewater treatment plant (WTP) on Pennypack Creek, an urban stream near Philadelphia, PA, increases nitrate concentrations to a mean of 8.5 mg-l-1 (as N). Concentrations decrease to 5.5 mg-l-1 about 7.5 km downstream. Reaches along this distance were sampled for nitrate concentration and delta-15N at fine spatial intervals to determine the reasons for this decrease. To quantify the effects of dilution, samples were collected from tributaries, groundwater springs, and upstream and downstream of tributaries or groundwater discharge zones identified through terrain analysis and continuous temperature modeling. These methods were also used to identify and sample reaches along which hyporheic flow occurred, where nitrate biological processing is often concentrated. In addition, loggers were installed at closely spaced sites to monitor daily fluctuations in nitrate, dissolved oxygen, and related parameters, which provided further indications of biological processing. Longitudinal sampling revealed decreases in nitrate concentration of 2 and 6.5 mg-l-1 during high and low flow, respectively. During high flow, delta-15N varied from 9.5 to 10.5 per mille downstream of the WTP, while delta-15N varied from 10.14 to 11.06 per mille throughout this reach during low flow. Mixing analysis indicated that groundwater discharge and biological processing both control nitrate concentration during both flow periods. Larger declines in nitrate concentration were observed during low flow than during high flow, and delta-15N fell between biological and groundwater signatures, indicating that both processes were enhanced. Continuous nitrate concentrations displayed distinct diurnal cycles often out-of-phase with dissolved oxygen cycles, indicating autotrophic processing. However, shifts occurred in nitrate cycle timing at a weekly scale wherein daily maximum concentrations were observed as many as 6 hours closer to noon than previously. These shifts were comparable to shifts observed across seasons in other studies, and by the end of the summer, nitrate and dissolved oxygen cycles were in-phase. Furthermore, shifts in nitrate cycles could not be linked to shifts in daily fluctuations of WTP discharge. Longitudinal sampling and continuous monitoring suggest that biological processing is an important control on nitrate concentrations in urban systems, though documenting its signature may be complicated by groundwater discharge and anthropogenic inputs. / Geology

Aevitas is an industrial wastewater treatment plant that receives about 300 m3/day of mixture of wastewater from different industries. The chemical oxygen demand of higher 600 ppm and the variety of the chemical constitution of industrial wastewater are two significant problems on Aevitas. Therefore, there is a strong need for developing advanced analytical techniques that can identify the specific compounds that are the source of COD. During 10 months, about 75 industrial samples were characterized using a battery of tests including GC/MS, COD, TOC, and pH to identify the chemicals that are main source of COD in the industrial wastewaters. Results showed that the COD of 87% of 75 provided samples from Aevitas plant was higher than 600. At the first step of process design, activated carbon was used to eliminate the identified organic chemicals from the wastewaters. The maximum and minimum of COD removal (depends on the chemical composition) of the wastewaters were obtained as 94 and 24%, respectively. Moreover, the amount of COD and TOC that can be adsorbed on the surface of 1 gram of the activated carbon were 25 and 7 mg, respectively. Although activated carbon is capable to reduce the COD, its capacity of adsorption is limited. To overcome this problem an alternative process, membrane filtration was applied for COD removal. Two types of crossflow NF (NF270, NF90, NFX, NFW, NFS, TS80, XN45, and SXN2_L) and RO (BW60 and TW30) membranes in two modules of the spiral wound and flat sheet were used. The filtration results of 11 different industrial wastewaters showed that NF90, TS80, NFX, and NFS were effective in COD removal. However, in terms of output flux NFX and NFS flat sheet were better than others were. Similar to the activated carbon process, the COD removal in filtration process was between 30 and 90%. The obtained results can be used to scale up the membrane filtration process at Aevitas. / Thesis / Master of Chemical Engineering (MChE) / Aevitas is an industrial wastewater treatment plant, which is situated at the City of Brantford. Every day, this plant receives about 15 trucks of the mixture of wastewaters from many different industries. The input wastewater into the plant should be treated and meet the environmental standard so that it can be discharged into a municipal wastewater plant. Currently, the maximum allowable chemical oxygen demand (COD) for discharging the treated wastewater from Aevitas to the municipal wastewater treatment plant is 600 ppm. Despite the fact, the current system in Aevitas is not efficient to meet this criterion. Thus, we strive to design efficient processes to overcome the problem. To this end, 75 samples were collected from Aevitas to observe the kind of chemicals that are the source of COD and then, two processes including activated carbon adsorption and membrane filtration were used for further reduction of COD. Although activated carbon can reduce the COD, the limited adsorption capacity was a major concern for its long-term application, especially if the COD of influent wastewater is higher than 2000 ppm. Membrane filtration was used as an alternative for activated carbon and the results showed that membrane could reduce the COD below 600 in 48% of the cases.

Septic tanks are utilized by many households across North America for wastewater treatment. Despite the economic and environmental importance of septic tanks, there has been limited innovation in septic tank design and research on the microbial communities responsible for wastewater treatment within these systems. InnerTube systems are septic tanks that employ a novel design to reduce solid accumulation in comparison to conventional septic tanks. For this project, 16S metabarcoding was employed to characterize conventional and InnerTube septic tank microbial communities and evaluate relationships between community composition, system design, and treatment efficacy. Wastewater was sampled along the length of InnerTubes to determine patterns of microbial succession and how they may impact InnerTube function. Wastewater was separated into liquid and solid fractions to identify differentially abundant taxa in each fraction. Populations of methylotrophic methanogens increased with distance from the InnerTube inlet. Solid communities were differentially more abundant in methanogens than liquid communities. Higher rates of solid degradation in InnerTubes may be due to longitudinal stratification of substrates and functionally distinct communities and the activity of methanogenic biomass. Septic tanks throughout Ontario were also surveyed to evaluate the effect of system design (conventional vs. InnerTube) and operational flow (single-pass vs. recirculation) on microbial community composition and to identify taxa correlated with chemical oxygen demand (COD) reduction. Single-pass InnerTube communities were more abundant in Pseudomonas which was attributed increased availability of long-chain fatty acid substrates. Recirculating conventional communities were more abundant in Arcobacter and Desulfomicrobium which was attributed to greater resistance to oxidative stress. Desulfovibrio and Brevundimonas were positively correlated with COD reduction. These putative hydrogen producers may facilitate greater COD reduction by forming syntrophic relationships with hydrogenotrophic methanogens. The findings of this project may be used to develop bioaugmentation inoculum, system designs, or operational strategies to optimize septic tank performance. / Thesis / Master of Science (MSc) / Septic systems (anaerobic digesters) are extensively used for on-site wastewater treatment. We evaluated the use of next-generation DNA sequencing to (1) assess the variability of septic system microbial communities and (2) to investigate relationships between communities and septic system type/performance. Microbial communities within septic systems were determined to be heterogeneous. Analyses also indicated that communities were highly variable between septic systems. Despite this variability, specific system types exhibited distinct microbial profiles. System performance was positively correlated with the abundance of hydrogen-producing bacteria. These results demonstrate the potential of next-generation DNA sequencing as a new tool to augment traditional wastewater analyses.

Optimal operation of water reclamation facilities (WRFs) is critical for an indirect potable reuse (IPR) system, especially when the reclaimed water constitutes a major portion of the reservoir's safe yield. It requires timely and informed decision-making in response to the fluctuating operational conditions, e.g., weather patterns, plant performance, water demand, etc. Advanced integrated modeling techniques can be used to develop reliable operational strategies to mitigate future risks associated with water quality without needing high levels of financial investment. The Upper Occoquan Service Authority (UOSA) WRF, located in northern Virginia, discharges nitrified reclaimed water directly into a tributary of the Occoquan Reservoir, one of the major water supply sources for Fairfax County. Among the many operational challenges at UOSA, one is to regulate the nitrate concentration in its reclaimed water based on the denitrifying capacity of the reservoir. This study presents an integrated model that is used to predict future reservoir conditions based on the weather and streamflow forecasts obtained from the Climate Forecast System and the National Water Model. The application captures the dynamic transformations of the pollutant loadings in the streams, withdrawals by the water treatment plant, WRF effluent flows, and plant operations to manage the WRF performance. It provides plant operators with useful feedback for correctly targeting the effluent nitrates using an intelligent process simulator called IViewOps. The platform is powered by URUNME, a new software that fully automates the operation of the reservoir and process models integrating forecasting products, and data sources. URUNME was developed in C#.NET to provide out-of-the-box functionality for model coupling, data storage, analysis, visualization, scenario management, and decision support systems. The software automatically runs the entire integrated model and outputs data on user-friendly dashboards, displaying historical and forecasting trends, on a periodic basis. This decision support system can provide stakeholders with a holistic view for the design, planning, risk assessments, and potential improvements in various components of the water supply chain, not just for the Occoquan but for any reservoir augmentation type IPR system. / Doctor of Philosophy / In an indirect potable reuse (IPR) system, reclaimed water from an advanced wastewater treatment facility is blended with a natural water source, such as a reservoir, to augment drinking water supply. Reliable operation of such a system is critical, especially when the reclaimed water constitutes a major portion of the withdrawals from the reservoir for treatment and distribution. One example of such an IPR system is the Upper Occoquan Service Authority (UOSA) water reclamation facility (WRF) which discharges its reclaimed water into the Occoquan Reservoir, a key water resource for Fairfax County. Integrated environmental modeling (IEM) provides a comprehensive approach towards the design and operation of water resource systems in which water supply, drainage, and sanitation are simulated as a single entity rather than independent units. In IEM, different standalone models, each representing a single subsystem, are linked together to analyze the complex interactions between various components of the system. This approach can be used for developing operational support tools for an IPR system to ensure timely and informed decision-making in response to the fluctuating conditions, e.g., weather patterns, plant performance, water demand, etc. The overarching goal of this research was to integrate different models and the data sources and develop a decision support system (DSS) to manage the UOSA-WRF performance. This resulting integrated model is used to predict future reservoir conditions based on the weather and streamflow forecasts obtained from the National Weather Service. The application runs various future scenarios to capture the possible variations of the pollutant loadings in the streams, withdrawals by the water treatment plant, WRF effluent flows, and plant operations and provide feedback to plant operators. The entire integrated model is operated periodically to output data on user-friendly dashboards, displaying historical and forecasting trends. The DSS provides stakeholders with a holistic view for the design, planning, risk assessments, and potential improvements in various components of the water supply chain, not just for the Occoquan but for any reservoir augmentation type IPR system.

Aerobic granular sludge has been regarded as a promising alternative to the conventional activated sludge which has been used for a century in that granular sludge offers advantages in high biomass retention, fast sludge-water separation, and small footprint requirement. However, this technology has been rarely applied in continuous flow reactors (CFRs) which are the most common type of bioreactors used in water resource recovery facilities across the world. Hence, the overarching goal of this study is to provide advanced understanding of biogranulation mechanism to enable industrial application of this technology. The lack of long-term stability study in CFRs has restricted its full-scale acceptability. The high settling velocity-based selection pressure has been regarded as the ultimate driving force towards biogranulation in sequential batch reactors (SBRs). In this study, this physical selection pressure was firstly weakened and then eliminated in CFRs to investigate its role in maintaining the long-term structural stability of aerobic granules. Given the fact that implementing settling velocity-based selection pressure only can cultivate biogranules in SBRs but not in completely stirred tank reactors (CSTRs), the essential role of feast/famine conditions was investigated. Seventeen sets of data collected from both literature and this study were analyzed to develop a general understanding of the granulation mechanisms. The outcome indicated that granulation is more sensitive to the feast/famine conditions than to the settling velocity-based selection pressure. The theory was tested in a CFR with 10-CSTR chambers connected in series to provide feast/famine conditions followed by a physical selector separating the slow-settling bioflocs and fast-settling biogranules into feast and famine zones, respectively. Along with successful biogranulation, the startup performance interruption problem inherent in SBRs was also resolved in this innovative design because the sludge loss due to physical washout selection was mitigated by returning bioflocs to the famine zone. Then, a cost-effective engineering strategy was put forward to promote the full-scale application of this advanced technology. With this generalized biogranulation theory, pure culture biogranules with desired functions for high value-added bioproducts were also investigated and achieved for the first time in this study, which paves a new avenue to harnessing granulation technology for intensifying waste valorization bioprocesses. / Doctor of Philosophy / Nowadays, the rapid population growth and unprecedented urbanization are overloading the capacity of many wastewater resource recovery facilities (WRRFs). Therefore, there is a need to develop a cost-effective strategy to upgrade the treatment capacity of existing WRRFs without incurring major capital investment. Because conventional activated sludge comes with loose structure and poor settleability, replacing them with dense aerobic granular sludge offers the opportunity to intensify the capacity of existing WRRF tankage and clarifiers through better retention of high bacterial mass that offers not only a fast pollutant removal rate but also a high water-solids separation rate. The aerobic granulation technology turns traditional activated sludge into granular sludge by inducing microbial cell-to-cell co-aggregation. Although this technology has been developed for more than 20 years, its application in full-scale WRRFs is still limited because majority of WRRFs are constructed with continuous flow reactors in which the aerobic granulation mechanism largely remains unknown. Besides, the long-term stability of aerobic granules in continuous flow reactors also remain unstudied, further constraining the full-scale application of the technology. The sensitivity of aerobic granulation to physical selection and biological selection was analyzed in this study. The results concluded that aerobic granulation is more sensitive to the latter but not to the former. Subsequently, this theory was tested in a novel bioreactor setup that creates feast/famine conditions for biological selection. A physical selector was installed at the end of the bioreactor to separate and return the fast- and slow- settling bioparticles to the feast and famine zones, respectively. This unique reactor design and operational strategy provided an economical approach to retrofitting current WRRFs for achieving treatment capacity upgrading without major infrastructure alternation. It also protected the bioreactor startup performance by enhancing the stability of WRRFs in the future application. Last but not least, this updated understanding of aerobic granulation theory was for the first time extrapolated to and verified with the formation of pure culture biogranules harnessed in this study for value-added bioproduct valorization from waste materials.

Sustainable tilapia production at Blue Ridge Aquaculture (BRA) is constrained by availability of high quality replacement water. I developed a pilot-scale wastewater treatment system to treat and reuse effluent presently discharged. An initial study was conducted to determine the response of the BRA waste stream to ozone application. Dosages of 6.9, 4.8 and 2.4 g O3 were applied for 30 minutes to 35 L of settled effluent. Optimum ozone dosage and reaction time, ozone transfer efficiency, ozone yield coefficient, degree of pollutant removal, and other ozone and water quality parameters were determined. Most results suggested that the maximum process feasibility limit for ozone contact time was approximately 9 minutes at an applied ozone concentration of 23g/m3 (6.9 g O3 dose). Formation of foam increased solids and COD removal up to three times. Poor removal or accumulation of DOC and TAN was observed, indicating the need for biological treatment following ozonation. Next, I evaluated a pilot station treatment train including sedimentation, microscreen filtration, fluidized bed denitrification, ozonation, aerobic biological oxidation in a trickling filter, and jar-test chemical flocculation. Significant improvements were found regarding solids, COD, cBOD5, NO3--N, TKN, and turbidity. Removal of foam after ozonation improved ozonation efficacy and pollutant removal. A nitrogen budget for the BRA facility was derived, indicating that 35% of the nitrogen applied in feed was assimilated in fish. I evaluated the possible impact of residual inorganic nitrogen forms from treated effluent upon fish in the recirculating systems. I found that less than 1% of the TAN produced would return the recovered stream, and that the existing biological contactors can remove it. Evaluation of TAN fate indicated that 84% was oxidized in biofilters, 14% was oxidized by passive nitrification, and 1% was removed by water exchange. For NO3-N, I determined that 56% was removed by passive denitrification and 44% by daily water exchange. The pilot station design was effective for removing organics and nutrients, and can serve as the basis for scale-up for treating and reusing the entire BRA effluent stream. / Ph. D.

Current treatment of wastewater can effectively remove the contaminants; however, the effluent is still not widely reused because of some undesired substances like pathogens and trace organic chemicals. To promote water reuse, membrane-based technologies have emerged as a robust and more efficient alternative to current treatment practice. Among these membrane processes, forward osmosis (FO) utilizes an osmotic pressure gradient across a semi-permeable membrane to reclaim high-quality water. Still, several key challenges remain to be addressed towards broader FO application, including energy-intensive draw regeneration to yield product water and salinity buildup in the feed solution. To bypass energy-intensive draw regeneration, commercial solid fertilizers was utilized as a regeneration-free draw solute (DS), harvesting fresh water towards direct agricultural irrigation. However, using nutrient-rich fertilizers as DS resulted in an elevated reverse solute flux (RSF). This RSF, known as the cross-membrane diffusion of DS to the feed solution, led to deteriorated solute buildup on the feed side, reduced osmotic driving force, increased fouling propensity, and higher operation cost. To effectively mitigate solute buildup while achieving energy-efficient water reclamation, a parallel electrodialysis (ED) device was integrated to FO for DS recovery in the feed solution. The salinity in the feed solution was consistently controlled below 1 mS cm-1 via the hybrid FO-ED system. Considering solute buildup is merely a consequence of RSF, direct control of RSF was further investigated via operational strategy (i.e., an electrolysis-assisted FO) and membrane modification (i.e., surface coating of zwitterion-functionalized carbon nanotubes). Significantly reduced RSF (> 50% reduction) was obtained in both approaches with minor energy/material investment. With two major bottlenecks being properly addressed for energy-efficient water reclamation, FO was further integrated with a microbial electrolysis cell (MEC) to achieve integrated nutrient-energy-water recovery from high-strength wastewater (i.e., the digestor centrate). The abovementioned research projects are among the earliest efforts to address multiple key challenges of FO during practical application, serving as a cornerstone to facilitate the transformation of current water/wastewater treatment plant to resource recovery hub in order to ensure global food-energy-water security. / Doctor of Philosophy / Exploring alternative water supply, for instance via reusing wastewater, will be essential to deal with the global water crisis. Current wastewater treatment can effectively remove the contaminants; however, the treated wastewater is still not widely reused due to the possible presence of residual contaminants. In recent years, membrane-based technologies have emerged as a promising treatment process to produce clean water. Among all available membrane technologies, forward osmosis (FO) takes advantage of the osmotic pressure difference across a special membrane to extract fresh water from a low-salinity FEED solution (for example, wastewater) to a high-salinity DRAW solution. The reclaimed fresh water can be reused for other applications. Still, the FO process is facing several critical challenges for broader applications. The first challenge is that additional energy is required to separate clean water from the diluted DRAW solution, leading to notably increased energy consumption for the FO process. To bypass this energy-intensive separation, commercial solid fertilizers was utilized as a separation-free DRAW solution for FO process. Once the clean water is extracted to the DRAW solution (fertilizer), the diluted fertilizer solution together with the fresh water can be directly used for agricultural irrigation. The second challenge is that, when fertilizer is applied as the DRAW solution, nutrient rich fertilizers can penetrate the FO membrane and escape to the FEED solution (wastewater). This phenomenon is known as the reverse solute flux (RSF). RSF can result in many adverse effects, such as wastewater contamination and increased operational cost. To prevent this, we used an additional device named electrodialysis to effectively recapture the “escaped” fertilizers in the FEED solution. Besides this indirect approach to recover escaped fertilizers, we also investigated direct approaches to control RSF, including operational strategy and membrane modification. With two major challenges being properly addressed for energy-efficient water reclamation, FO was further combined with a microbial electrolysis cell (MEC) to achieve multiple resource recovery from wastewater, including water, nutrient, and energy components. The above mentioned research projects are among the earliest efforts to address multiple key challenges of FO during water and resource recovery from wastewater to ensure global food-energy-water security.

Many industrial processes would require enormous amounts of water, which could ultimately result in wastewater. Water scarcity in many parts of the world makes this situation unsustainable. In order to reuse wastewater in industrial processes or for other purposes, wastewater must be treated properly. In industrial wastewater treatment, electrocoagulation-flotation (ECF) can be used to dissolve sacrificial electrodes and produce metal coagulant in-situ by applying a current to the electrodes. The reactor design and electrode configuration can profoundly affect the performance of electrocoagulation-flotation (ECF). While most conventional ECF reactors use an open-vertical electrode configuration in rectangular cells, mixing is limited by vertical electrodes that make a barrier and disrupt the flow hydrodynamics. The effects of these factors may influence removal efficiency, flow hydrodynamic, floc formation, and flotation/settling characteristics. The present work aimed to optimize the ECF process by developing an innovative electrode configuration. A variety of parameters were examined to determine the effectiveness of the removal of contaminants from industrial wastewater that had turbidity, emulsified oil, and heavy metals (Si, Zn, Pb, Ni, Cu, Cr, and Cd), as well as stirring speed and foaming. Additionally, the experimental results of the innovative electrode configuration were compared with those of the conventional rectangular cell with plate electrode configuration. Based on the results, the innovative electrode configuration consumed approximately 20% less energy than a conventional ECF for operating times of 10, 20, 30, 32, 48, and 70 minutes. As a result of the enhanced flow hydrodynamic, the formed gas bubbles tilted toward the center, significantly reducing foam formation. There was also an investigation of the dominant operating parameters for electrocoagulation-flotation (ECF) that could affect the removal efficiency, including current density (CD), initial pH, electrolytic conductivity, dosage of coagulant, operating time, initial turbidity concentration, and stirring speed. In addition, a novel approach has been proposed for evaluating EC performance and selecting an appropriate process for removing sludge based on the intake's initial concentration. Keywords: Electrode configuration, electrocoagulation process, electro-flotation, energy consumption, removal efficiency, Electrochemical treatment, Aluminium electrode, Turbidity removal, TOC removal, operating parameters, computational fluid dynamics, Reynolds number, mass transfer, pH evolution.:Table of Contents Abstract 7 1. Introduction 16 1.1. The electrocoagulation process 17 1.2. Problem statement 19 1.3. Objectives 20 1.4. Scope of the work 21 2. Literature survey 23 2.1. Industrial wastewater and treatment methods 24 2.1.1. Impact of industrial growth 24 2.1.2. An analysis of global industrial growth based on statistics 25 2.1.3. Extensive sources of industrial effluent 26 2.1.4. Wastewater and reserve rehabilitation in industry 34 2.1.5. Applied techniques in industrial wastewater treatment 40 2.2. Electrocoagulation (ECF) 50 2.3. Comparison of EC with other treatment methods 50 2.4. Basic concepts and theory of coagulation and electrocoagulation 53 2.5. Electrocoagulation applications 58 2.5.4. Textile industry 60 2.5.5. Leather Tanning Industry 61 2.5.6. Metal-bearing industrial effluents 61 2.5.7. Pulp and paper industry 62 2.5.8. Petroleum refinery 63 2.6. Type and Configuration of the Electrodes 64 2.6.1. Case of Al electrodes 66 2.6.2. Case of Fe electrodes 68 2.7. Reactor design 71 2.6. Modeling 72 2.6.1. Kinetics 73 2.7. Impact of electrocoagulation operating condition on contaminant removal efficiency 75 2.7.1. Effect of current density 75 2.7.2. Effect of initial pH 75 2.7.3. Effect of operating time 76 2.7.4. Effect of electro conductivity 76 2.7.5. Effect of stirring speed 77 2.7.6. Effect of concentration 77 2.7.7. Effect of gap between the electrodes 77 2.7.8. Effect of temperature 78 2.8. Economical aspects and cost analysis 78 3. Material and methods of the tests 80 3.1. Test procedure 1: Impact of operating parameters on removal of turbidity 81 3.1.1. Operating conditions 81 3.1.2. EC cell construction and electrode arrangement 82 3.1.3. Synthetic wastewater 85 3.1.4. Analytical methods and EC procedure 86 3.1.5. Anodic and cathodic reactions 87 3.1.6. Electrical double layer and particle stability 89 3.2. Test procedure 2: Spiral electrode configuration 91 3.2.1. Experimental Setup 91 3.2.2. Sampling and analytical measurements 95 3.2.3. Experimental procedure 95 4. Results and discussion 97 4.1. Test procedure 1: Impact of operating parameters on removal of turbidity 98 4.1.1. Effect of current density (CD) 98 4.1.2. Effect of initial pH 100 4.1.3. Effect of electrolytic conductivity 104 4.1.4. Effect of coagulant dosage, electrode and energy consumption 106 4.1.5. Effect of current density and operating time on initial turbidity concentration 107 4.1.6. Effect of stirring speed 111 4.1.7. Effect of electrode passivation 112 4.2. Test procedure 2: Spiral electrode configuration 115 4.2.1. Removal efficiency of contaminants 115 4.2.2. Effect of stirring speed and ECF configuration on removal efficiency 119 4.2.3. Energy consumption and voltage rise 123 4.2.4. Foaming effect 126 4.3. Computational Fluid Dynamics (CFD) Simulation 128 5. Conclusions and future work 138 5.1. Conclusions 139 5.2. Future works 142 References 143 6. Appendix 159