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Description
The high levels of pollution associated with mining activities necessitate more efficient methods of treating mining effluent before it is released into the environment. Phosphate -mining wastewater contains high concentrations of sulfate that can be removed and recovered as elemental sulfur (S0), which is a useful resource. The Membrane Biofilm Reactor (MBfR) uses gas-transfer membranes for the delivery of gases to microorganisms that carry out oxidation-reduction reactions that lead to the breakdown of contaminants. The two main microorganisms involved in the treatment of sulfate wastewater using the MBfR are sulfate-reducing bacteria (SRB) for the reduction of sulfate into sulfide and sulfur-oxidizing bacteria (SOB) for the oxidation of sulfide into S0. In this work, the kinetic processes involved in sulfate reduction and sulfide oxidation for SRB and SOB were modeled using the steady-state biofilm model and mass balances on a completely mixed biofilm reactor. The model results identified trends of substrate removal, biofilm accumulation, and hydraulic retention time (HRT) for the design of the sulfate-treatment system. The HRT required for 97.5% sulfate removal was about 0.1 d and that for 97.5% sulfide removal about 0.2 d. Higher levels of biofilm accumulation occurred with sulfide oxidation due to the larger biomass yield of the SOB. The needed delivery of H2 gas required for sulfate reduction and O2 gas for sulfide oxidation, as well as the alkalinity changes, also were determined based on the removal levels.
ContributorsAppiah Nsiah, Gloria (Author) / Rittmann, Bruce BER (Thesis advisor) / Abbaszadegan, Morteza (Committee member) / Fox, Peter (Committee member) / Arizona State University (Publisher)
Created2021
Description
In the present study, primarily, gas diffusion layer samples containing microporous layers (MPLs), are fabricated using carbon paper substrate, PUREBLACK® carbon powder and polyethylene glycol (PEG) as pore forming agent. The GDLs are studied in single cell fuel cell, to evaluate the effect of porosity of the micro-porous layer on the performance at different operating relative humidity conditions and compared with commercial GDLs. Scanning electron microscopy (SEM) and contact angle measurements indicate crack-free surface morphology and hydrophobic characteristics of the PUREBLACK® based GDLs, respectively. By varying the wt. % of PEG, fuel cell performance is evaluated under relative humidity conditions of 60 and 100 % using H2/O2 and H2/Air at 70 oC and the durability is also evaluated for the samples without, with 30% PEG and commercial. The fuel cell performance of the GDL with 30 % PEG (with pore volume 1.72 cc.g-1) exhibited higher performance (444 and 432 mW.cm-2 at 60 and 100 % RH conditions, respectively using H2 and air) compared to that without pore forming agent (436 and 397 mW.cm-2).Subsequently, the best performing configuration underwent two different ex-situ methods of accelerated stress testing (AST), in water and hydrogen peroxide (30%), for 1000 and 24 h, respectively. The samples were evaluated via contact angle, SEM, and fuel cell performance, before and after the ASTs, and compared to similar configuration, using carbon powder VULCAN® (XC-72R), and aged in the exact same conditions. Contact angle and SEM demonstrated greater degradation of VULCAN® carbon, especially in hydrogen peroxide, where carbon corrosion caused surface cracks and change in hydrophobicity. The fuel cell performance and durability, evaluated at 60 and 100% RH at 70 oC, using O2 and air as oxidants, confirmed that VULCAN® carbon is more prone to carbon corrosion, with significant performance loss (12-19%) in contrast to PUREBLACK® that demonstrated higher carbon corrosion resistance due to its graphitized surface.
ContributorsAthanasaki, Grigoria (Author) / Kannan, Arunachala Mada A. M. (Thesis advisor) / Nam, Changho (Committee member) / Peng, Xihong (Committee member) / Arizona State University (Publisher)
Created2021
Description
Microalgae offer a unique set of promises and perils for environmental management and sustainable production. Algal blooms are becoming a more frequent phenomenon within water infrastructure. As algae blooms are common, water infrastructure across the world has seen mounting problems associated with algal blooms. Some of these problems include biofouling and release of toxins. Since 1997, Arizona’s Central Arizona Project (CAP) has faced escalating problems associated with the algae diatom Cymbella sp. and the green-algae Cladophora glomerata. In this research study, algae are diagramed within the CAP system, the nutrient and abiotic requirements of the diatom Cymbella sp. are determined, and real-time microbial sensors are deployed along the CAP canals for understanding algae blooms and changes in CAP flow conditions. The following research objectives are met: How can water delivery infrastructure improve algae contamination risks in critical water resources?
To do this research demonstrates that (i) nuisance algae species within the CAP canals are Cymbella sp. and Cladophora glomerata (ii) that the nuisance “rock-snot” diatom Cymbella sp. is not Cymbella mexicana nor is it Cymbella janischii, but rather a novel Cymbella sp.(iii) that in laboratory settings, Cymbella sp. prefers high Phosphorus and low Nitrogen conditions (iv) that the Cymbella sp. bloom happens in the early summer along the CAP canals (v) that the diatom Cymbella sp. can be removed through chemical treatments (vi) that microbial sensors can measure changes in algae composition along the CAP canals (vii) that microbial sensors, water quality parameters, and weather data can be integrated to measure algae blooms within water systems.
ContributorsMeyer, Harrison (Author) / Weiss, Taylor (Thesis advisor) / Neuer, Suzanne (Committee member) / Abbaszadegan, Morteza (Committee member) / Arizona State University (Publisher)
Created2021
Description
Halogens in drinking water sources, such as bromine (Br) and iodine (I) pose no direct health risk, but are critical precursors in formation of cyto- and genotoxic brominated and iodinated (Br-/I-) DBPs. However, few spatial or historic datasets exist for bromine and iodine species in drinking water sources. This dissertation aims to quantify and understand the occurrence and speciation of Br and I in groundwater and surface water serving as source waters for drinking water treatment plants (DWTPs). Aggregation of data from >9000 non-drinking water sampling locations in USA collected from 1930-2017 on halides (bromide (Br-) and iodide (I-)) determined that Br- concentrations were 50 μg/L and 100 μg/L; and I- concentrations were 12 μg/L and 13 μg/L in surface and groundwater respectively. Although, these locations were not drinking water sources, this first of its kind analysis provides potential bounds for Br- and I-. To focus specifically on DWTP sources, a nationwide survey of >250 drinking water sources was conducted between 2018-2020. Br- ion is the only bromine specie, whereas both inorganic (iodide and iodate ions) and organic iodine occur. I- concentrations ranged from 1-250 μg/L and are 4 to 100 times lower than Br- concentrations (10-7800 μg/L, median=80 μg/L). No strong correlation exists between bromide and iodide occurrence (R<0.5, p<0.005). I- was detected in 50% of the samples (75th percentile=5 μg/L) and IO3- was detected in 40% (75th percentile=3 μg/L) of all the samples. To quantify iodine species, tandem ion chromatography and inductively coupled plasma mass spectrometry was applied for the first time in drinking water sources. I- and IO3- peaks were well resolved and have minimum detection limit of 0.4 μg/L and 0.7 μg/L respectively. Organic iodine (Org-I) peaks in select drinking water samples from the nationwide survey were partically resolved ranging from <5 to 40 μg/L. This dissertation provides updated nationwide Br- survey and first ever national I species survey. The data generated through this dissertation will be useful to further Br-/I-DBP formation and toxicity research by providing relevant drinking water sources information. Future research targeting Br- and I- removal is advocated for managing Br-/I-DBPs in watersheds.
ContributorsSharma, Naushita (Author) / Westerhoff, Paul (Thesis advisor) / Karanfil, Tanju (Committee member) / Herckes, Pierre (Committee member) / Lackner, Klaus (Committee member) / Arizona State University (Publisher)
Created2021
Description
Nearly 2.1 billion people around the world to date do not have access to safe drinking water. This study proposes a compact (2-L) upflow photoreactor that uses widely available photocatalysts material, such as titanium dioxide (TiO2) or hexagonal boron nitrate (hBN), to oxidize toxic micropollutants. Photocatalysts, such as TiO2, can create powerful hydroxyl radicals (OH•) under UV irradiation to oxidize and disinfect water with various toxic pollutants present in untreated waters. The study assesses this along with few other photoreactors in terms of their performance with an indicator dye, such as methyl orange (MO), para-chlorobenzoic acid (pCBA), as an intermediate of pesticides, and perfluorooctanoic acid (PFOA), part of the per- and polyfluoroalkyl substances (PFAS), a highly persistent organic contaminant in water. This study also describes the various stages of evolution of this 2-L photoreactor, first using TiO2 coated sand in maintaining a uniform (photocatalyst) bed in suspension along with few other modifications that resulted in a photoreactor with a 3 to 4-fold increase in contact time, is discussed. The final stage of this upflow photoreactor modification resulted in the direct use of photocatalysts as a slurry, which was critical, especially for hBN, which cannot be coated onto the sand particles. During this modification and assessment, a smaller bench-top photoreactor (i.e., collimated beam) was also built and tested. It was primarily used in screening various photocatalysts and operational conditions before assessment at this upflow photoreactor and also at a commercial photoreactor (Purifics Photo-Cat) of a larger scale. Thus, the overall goal of this study is to compare a few of these photoreactors of different designs and scales. This includes a collimated beam (at bench-scale), upflow photoreactor (at testbed scale), and a commercial photoreactor, Photo-Cat (at pilot-scale). This study also discusses the performance of these photoreactors under different operating conditions, which includes evaluating two different photocatalyst types (TiO2 and hBN), variable loading rates, applied UV doses, environment pH, and supplemental peroxide addition (as AOP) and with corresponding EEO values.
ContributorsCao, Jiefei (Author) / Sinha, Shahnawaz (Thesis advisor) / Westerhoff, Paul (Committee member) / Ersan, Mahmut (Committee member) / Arizona State University (Publisher)
Created2021
Description
The ongoing COVID pandemic has opened the doors for the development of effective surface disinfection technologies. UV technology is one of the most effective technique to be used in combination with different photocatalytic agents such as Titanium Dioxide (TiO2) for microbial inactivation. There are many bacteria and viruses which have the potential to infect humans via surface-oral/inhalation pathway. Thus, it is important to evaluate the effectiveness of these techniques used to inactivate microorganisms to minimize environmental transmission. UV light directly acts on bacteria and viruses by damaging their nucleic acids and protein structures. TiO2 acts as a photocatalyst, generates hydroxyl radicals under UV, leading to enhanced inactivation efficacy. This study focuses on the impact of UVC light at 254 nm wavelength in combination with spray formulations with TiO2 for the inactivation of E. coli (exposure times of 1, 5 and 10 minutes) and bacteriophages P22 (exposure times of 5 and 10 minutes) and MS2 (exposure times of 1 and 5 minutes). This study includes tests that explored the long-lasting impact of spray formulations on non-porous surface. Minimal inactivation of ~ 0.15 log inactivation of E. coli was resulted using TiO¬2 alone but when UV was added to the procedure on average 3 log inactivation was achieved. It was noted that MS2 was found to be more susceptible to UV as compared to P22 due to its higher inactivation rate. The spray formulation homogeneity is a critical factor in consistent microbial inactivation. In addition, the UV intensity of the handheld device is an important factor for total disinfection. However, the combined spray formulation and UV technology is an effective method of surface disinfection.
ContributorsBaxi, Dhatri Kamleshbhai (Author) / Abbaszadegan, Morteza (Thesis advisor) / Fox, Peter (Committee member) / Alum, Absar (Committee member) / Arizona State University (Publisher)
Created2021
Description
Water is a vital resource, and its protection is a priority world-wide. One widespread threat to water quality is contamination by chlorinated solvents. These dry-cleaning and degreasing agents entered the watershed through spills and improper disposal and now are detected in 4% of U.S. aquifers and 4.5-18% of U.S. drinking water sources. The health effects of these contaminants can be severe, as they are associated with damage to the nervous, liver, kidney, and reproductive systems, developmental issues, and possibly cancer. Chlorinated solvents must be removed or transformed to improve water quality and protect human and environmental health. One remedy, bioaugmentation, the subsurface addition of microbial cultures able to transform contaminants, has been implemented successfully at hundreds of sites since the 1990s. Bioaugmentation uses the bacteria Dehalococcoides to transform chlorinated solvents with hydrogen, H2, as the electron donor. At advection limited sites, bioaugmentation can be combined with electrokinetics (EK-Bio) to enhance transport. However, challenges for successful bioremediation remain. In this work I addressed several knowledge gaps surrounding bioaugmentation and EK-Bio. I measured the H2 consuming capacity of soils, detailed the microbial metabolisms driving this demand, and evaluated how these finding relate to reductive dechlorination. I determined which reactions dominated at a contaminated site with mixed geochemistry treated with EK-Bio and compared it to traditional bioaugmentation. Lastly, I assessed the effect of EK-Bio on the microbial community at a field-scale site. Results showed the H2 consuming capacity of soils was greater than that predicted by initial measurements of inorganic electron acceptors and primarily driven by carbon-based microbial metabolisms. Other work demonstrated that, given the benefits of some carbon-based metabolisms to microbial reductive dechlorination, high levels of H2 consumption in soils are not necessarily indicative of hostile conditions for Dehalococcoides. Bench-scale experiments of EK-Bio under mixed geochemical conditions showed EK-Bio out-performed traditional bioaugmentation by facilitating biotic and abiotic transformations. Finally, results of microbial community analysis at a field-scale implementation of EK-Bio showed that while there were significant changes in alpha and beta diversity, the impact of EK-Bio on native microbial communities was minimal.
ContributorsAltizer, Megan Leigh (Author) / Torres, César I (Thesis advisor) / Krajmalnik-Brown, Rosa (Thesis advisor) / Rittmann, Bruce E (Committee member) / Kavazanjian, Edward (Committee member) / Delgado, Anca G (Committee member) / Arizona State University (Publisher)
Created2020
Description
The intent of this dissertation was to advance the knowledge of the impacts of building design and use on the quality of the potable water. Fluctuations in water use by occupants and equipment can cause stagnant conditions that causes water quality decay such as loss of chlorine disinfectant, an increase in microorganism and pathogen growth, an increase in metals concentrations, and an increase in disinfection byproducts. The United States Environmental Protection Agency has drinking water standards for distribution systems, but these standards stop at the meter with exception of the Lead and Copper Rule. There are also building codes to ensure proper plumbing materials are used that come in contact with potable water. However, neither standards nor codes require building water quality monitoring. Therefore, monitoring the building potable water system is an important aspect of building water quality that is not done on a large scale.Chapter 2 investigated how water quality evolved in a “green”, multi-story, institutional building during the first 6 months of building life. The results indicated that Wi-Fi logins could be used to correlate occupancy activity and copper (Cu) concentrations in water. As occupancy activity increased, Cu concentrations decreased. However, chlorine (Cl2) residual (or free chlorine) was only measurable twice at two kitchen sinks via grab sampling during the duration of the 6-month study regardless of occupancy activity.
Chapter 3 provided improved understanding of how to carry out effective building water sampling (e.g., grab samples vs real time) and which water quality parameters were most influenced by the building water system during the first year of occupancy in relation to municipal water quality. The results showed the temperature (T), pH, UVA254, a surrogate for organic matter, cellular adenosine triphosphate (cATP), trihalomethanes (THMs), and Cu were always greater inside the building than at building entry while free Cl2 was always lower inside the building than at the building entry.
Chapter 4 investigated a remedial flushing program for three schools. Overall, the study showed the quality of water does change after a flushing event. Free Cl2 was reestablished, and metals concentrations decreased. However, equipment flushing, such as hot water heaters, may be necessary to fully remediate Legionella. Lastly, one-time flushing is most likely a temporary solution. A more routine approach to building flushing and monitoring may be necessary until normal or sustained occupancy resumes.
ContributorsRichard, Rain (Author) / Boyer, Treavor H (Thesis advisor) / Hamilton, Kerry A (Committee member) / Ross, Heather M (Committee member) / Arizona State University (Publisher)
Created2021
Description
Large-scale cultivation of photosynthetic microorganisms for the production of biodiesel and other valuable commodities must be made more efficient. Recycling the water and nutrients acquired from biomass harvesting promotes a more sustainable and economically viable enterprise. This study reports on growing the cyanobacterium Synechocystis sp. PCC 6803 using permeate obtained from concentrating the biomass by cross-flow membrane filtration. I used a kinetic model based on the available light intensity (LI) to predict biomass productivity and evaluate overall performance.
During the initial phase of the study, I integrated a membrane filter with a bench-top photobioreactor (PBR) and created a continuously operating system. Recycling permeate reduced the amount of fresh medium delivered to the PBR by 45%. Biomass production rates as high as 400 mg-DW/L/d (9.2 g-DW/m2/d) were sustained under constant lighting over a 12-day period.
In the next phase, I operated the system as a sequencing batch reactor (SBR), which improved control over nutrient delivery and increased the concentration factor of filtered biomass (from 1.8 to 6.8). I developed unique system parameters to compute the amount of recycled permeate in the reactor and the actual hydraulic retention time during SBR operation. The amount of medium delivered to the system was reduced by up to 80%, and growth rates were consistent at variable amounts of repeatedly recycled permeate. The light-based model accurately predicted growth when biofilm was not present. Coupled with mass ratios for PCC 6803, these predictions facilitated efficient delivery of nitrogen and phosphorus. Daily biomass production rates and specific growth rates equal to 360 mg-DW/L/d (8.3 g/m2/d) and 1.0 d-1, respectively, were consistently achieved at a relatively low incident LI (180 µE/m2/s). Higher productivities (up to 550 mg-DW/L/d) occurred under increased LI (725 µE/m2/s), although the onset of biofilm impeded modeled performance.
Permeate did not cause any gradual growth inhibition. Repeated results showed cultures rapidly entered a stressed state, which was followed by widespread cell lysis. This phenomenon occurred independently of permeate recycling and was not caused by nutrient starvation. It may best be explained by negative allelopathic effects or viral infection as a result of mixed culture conditions.
During the initial phase of the study, I integrated a membrane filter with a bench-top photobioreactor (PBR) and created a continuously operating system. Recycling permeate reduced the amount of fresh medium delivered to the PBR by 45%. Biomass production rates as high as 400 mg-DW/L/d (9.2 g-DW/m2/d) were sustained under constant lighting over a 12-day period.
In the next phase, I operated the system as a sequencing batch reactor (SBR), which improved control over nutrient delivery and increased the concentration factor of filtered biomass (from 1.8 to 6.8). I developed unique system parameters to compute the amount of recycled permeate in the reactor and the actual hydraulic retention time during SBR operation. The amount of medium delivered to the system was reduced by up to 80%, and growth rates were consistent at variable amounts of repeatedly recycled permeate. The light-based model accurately predicted growth when biofilm was not present. Coupled with mass ratios for PCC 6803, these predictions facilitated efficient delivery of nitrogen and phosphorus. Daily biomass production rates and specific growth rates equal to 360 mg-DW/L/d (8.3 g/m2/d) and 1.0 d-1, respectively, were consistently achieved at a relatively low incident LI (180 µE/m2/s). Higher productivities (up to 550 mg-DW/L/d) occurred under increased LI (725 µE/m2/s), although the onset of biofilm impeded modeled performance.
Permeate did not cause any gradual growth inhibition. Repeated results showed cultures rapidly entered a stressed state, which was followed by widespread cell lysis. This phenomenon occurred independently of permeate recycling and was not caused by nutrient starvation. It may best be explained by negative allelopathic effects or viral infection as a result of mixed culture conditions.
ContributorsThompson, Matthew (Author) / Rittmann, Bruce E. (Thesis advisor) / Fox, Peter (Committee member) / Krajmalnik-Brown, Rosa (Committee member) / Arizona State University (Publisher)
Created2015
Description
Global shortages of urea and unsustainable production of synthetic urea have caused concerns over the future of food production, automobile operation, and other processes. Urine is a waste product that could supplement synthetic urea production. This study utilizes polyamide reverse osmosis (RO) and nanofiltration (NF) membranes in a cross-flow orientation to selectively recover urea from fresh human urine. Urea permeation experiments were conducted to determine the effects of urea stabilization via pH adjustment and membrane type on the production of a pure urea product. Fouling mitigation experiments were then conducted to determine the efficacy of microfiltration (MF) pretreatment on the reduction of the membrane fouling layer. The results showed that the NF90 membrane had advantageous performance to the BW30 RO and NF270 membranes, permeating 76% of the urea while rejecting 68% of the conductivity. Urine stabilization via acetic acid or sodium hydroxide addition did not inhibit membrane performance, signifying the use of pH 5 as a suitable pretreatment condition. Real fresh urine had higher rejection of constituents for NF90, suggesting the reduction of flux across the membrane due to interactions with organic material. MF pretreatment reduced foulant thickness and permeate flux loss but did not change the speciation of microorganisms. Finally, different urea-based products, such as fertilizers, biocement, and synthetic polymers, were suggested to show the potential of urine-recovered urea to reduce costs. The results from this work show the efficacy of using polyamide RO and NF membranes to supplement unsustainable synthetic production of urea with sustainably sourced urea from a waste product, human urine.
ContributorsCrane, Lucas Christopher (Author) / Boyer, Treavor H (Thesis advisor) / Perreault, Francois (Committee member) / Westerhoff, Paul (Committee member) / Arizona State University (Publisher)
Created2022