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Description
To further the efforts producing energy from more renewable sources, microbial electrochemical cells (MXCs) can utilize anode respiring bacteria (ARB) to couple the oxidation of an organic substrate to the delivery of electrons to the anode. Although ARB such as Geobacter and Shewanella have been well-studied in terms of their microbiology and electrochemistry, much is still unknown about the mechanism of electron transfer to the anode. To this end, this thesis seeks to elucidate the complexities of electron transfer existing in Geobacter sulfurreducens biofilms by employing Electrochemical Impedance Spectroscopy (EIS) as the tool of choice. Experiments measuring EIS resistances as a function of growth were used to uncover the potential gradients that emerge in biofilms as they grow and become thicker. While a better understanding of this model ARB is sought, electrochemical characterization of a halophile, Geoalkalibacter subterraneus (Glk. subterraneus), revealed that this organism can function as an ARB and produce seemingly high current densities while consuming different organic substrates, including acetate, butyrate, and glycerol. The importance of identifying and studying novel ARB for broader MXC applications was stressed in this thesis as a potential avenue for tackling some of human energy problems.
ContributorsAjulo, Oluyomi (Author) / Torres, Cesar (Thesis advisor) / Nielsen, David (Committee member) / Krajmalnik-Brown, Rosa (Committee member) / Popat, Sudeep (Committee member) / Arizona State University (Publisher)
Created2013
Description
In our modern world the source of for many chemicals is to acquire and refine oil. This process is becoming an expensive to the environment and to human health. Alternative processes for acquiring the final product have been developed but still need work. One product that is valuable is butanol. The normal process for butanol production is very intensive but there is a method to produce butanol from bacteria. This process is better because it is more environmentally safe than using oil. One problem however is that when the bacteria produce too much butanol it reaches the toxicity limit and stops the production of butanol. In order to keep butanol from reaching the toxicity limit an adsorbent is used to remove the butanol without harming the bacteria. The adsorbent is a mesoporous carbon powder that allows the butanol to be adsorbed on it. This thesis explores different designs for a magnetic separation process to extract the carbon powder from the culture.
ContributorsChabra, Rohin (Author) / Nielsen, David (Thesis director) / Torres, Cesar (Committee member) / Barrett, The Honors College (Contributor) / Chemical Engineering Program (Contributor)
Created2015-05
Description
Alternative ion exchange membranes for implementation in a peroxide production microbial electrochemical cel (PP-MEC) are explored through membrane stability tests with NaCl electrolyte and stabilizer EDTA at varying operational pHs. PP-MEC performance parameters \u2014 H2O2 concentration, current density, coulombic efficiency and power input required \u2014 are optimized over a 7 month continuous operation period based on their response to changes in HRT, EDTA concentration, air flow rate and electrolyte. I found that EDTA was compatible for use with the membranes. I also determined that AMI membranes were preferable to CMI and FAA because it was consistently stable and maintained its structural integrity. Still, I suggest testing more membranes because the AMI degraded in continuous operation. The PP-MEC produced up to 0.38 wt% H2O2, enough to perform water treatment through the Fenton process and significantly greater than the 0.13 wt% batch PP-MEC tests by previous researchers. It ran at > 0.20 W-hr/g H2O2 power input, ~ three orders of magnitude less than what is required for the anthraquinone process. I recommend high HRT and EDTA concentration while running the PP- MEC to increase H2O2 concentration, but low HRT and low EDTA concentration to decrease power input required. I recommend NaCl electrolyte but suggest testing new electrolytes that may control pH without degrading H2O2. I determined that air flow rate has no effect on PP-MEC operation. These recommendations should optimize PP-MEC operation based on its application.
ContributorsChowdhury, Nadratun Naeem (Author) / Torres, Cesar (Thesis director) / Popat, Sudeep (Committee member) / Chemical Engineering Program (Contributor) / Barrett, The Honors College (Contributor)
Created2016-05
Description
Selenium oxyanions (i.e., selenate and selenite) can be released into the environment from surface mining. Selenium is an essential micronutrient, but high selenium in water has adverse health effects for aquatic animals and humans. Mine-influenced water is often co-contaminated with high concentrations of nitrate, selenium oxyanions, and sulfate. The Saturated Rock Fill (SRF) is a treatment technology that utilizes waste rocks from surface mining to create a biological treatment system that can be effective at removing nitrate and selenium-oxyanions from the mine-influenced water. The Selenium, Sulfur, and Nitrogen species (SeSANS) model can be used to estimate the respiration, synthesis, and endogenous decay of biomass in an SRF. The goal of this thesis is to simulate SRF biofilms using a biofilm version of SeSANS. Three nitrate loads (100, 250, and 450 kg NO3-N/day) with a low flow rate (1000 m3/d) or a high flow rate (5000 m3/d) -- a total of six scenarios -- were simulated for 5000 days of operation. The influent water contained 0.18 g Se/m3 of selenate, 0.02 Se/m3 selenite, and 800 S/m3 of sulfate; the input nitrate concentration was 100, 250, and 450 g N/m3 for the low flow rate and 20, 50, and 90 g N/m3 for the high flow rate. Methanol was injected as the electron donor. These criteria were used to define a successful simulation: effluent nitrate < 3 mg N/L and total dissolved Se < 0.029 mg Se/L, minimal sulfate reduction, and an average biofilm-biomass density of 96 kg TS/m3. To achieve those criteria, the following model parameters were adjusted: rate for methanol addition, biofilm thickness, SRF volumes, and biofilm-detachment rates. The most important parameter for achieving all the goals was the methanol addition ratio: 3.56 g COD/g NO3-N. Another important outcome was that the high-flow-rate scenarios required a larger total SRF volume to achieve target nitrate and Se-oxyanion reductions. The results of the simulations can be used to estimate biofilm characteristics and optimize the SRF configuration and treatment operation.
ContributorsKuo, Jacqueline (Author) / Rittmann, Bruce E (Thesis advisor) / Boltz, Joshua P (Committee member) / Torres, Cesar (Committee member) / Arizona State University (Publisher)
Created2023
Description
The world currently faces hundreds of millions of cubic meters of soil contaminated with petroleum crude oil residuals. The application of ozone gas (O3) to contaminated soil is an effective means to oxidize petrogenic compounds and, when used with bioremediation, remove the oxidized byproducts. The overarching goal of this dissertation was to evaluate two areas of potential concern to large-scale O3 deployment: the capacity of O3-treated petroleum contaminated soils to support seed germination before bioremediation and the transport characteristics of O3 in soil columns. A matched study comparing the germination outcomes of radish (Raphanus sativus L.), grass (Lagurus ovatus), and lettuce (Lactuca sativa) in soils contaminated with three crude oils at various O3 total-dose levels showed that radish germination was sensitive to the soluble byproducts of oxidized petroleum (assayed as dissolved organic carbon [DOC]), but not sensitive to the unreacted petroleum (total petroleum hydrocarbon [TPH]). A multivariable logistic regression model based on the radish results showed that adverse germination outcomes varied with the DOC concentration and that DOC ecotoxicity decreased with increasing O3 dose-level and background organic material. The model was used to create a risk management map of conditions that created 10%, 25%, and 50% extra risks of adverse radish germination. Thus, while O3 effectively lowered TPH in soils, the byproducts exhibited ecotoxicity that inhibited radish germination. On the other hand, the sensitivity of radish germination to oxidized petroleum byproducts could be utilized to assess ecological risk. The feasibility of gas transport in the soil matrix is also of paramount concern to field-scale utilization of O3. A matched study comparing TPH removal at three field-relevant loading rates (4, 12, or 36 mgozone/ gsoil/ hr) and various total dose-levels showed an anisotropic pattern along the axial distance favoring the column inlet end. The asymmetry decreased as loading rate decreased and with concurrent improvements in O3-transport distance, O3 utilization, and heat balance. Overall, a low O3 loading rate significantly improved O3 transport and utilization efficiency, while also better distributing reaction-generated heat along the gas flow path for a depth typically utilized in bioremediation field settings.
ContributorsYavuz, Burcu Manolya (Author) / Rittmann, Bruce E (Thesis advisor) / Delgado, Anca G (Committee member) / Westerhoff, Paul (Committee member) / Arizona State University (Publisher)
Created2022
Description
The increasing concentrations of greenhouse gases into the atmosphere call for urgent measures to use non-fossil feedstock for fuels and chemicals. Synthesis gas (or syngas) is a mixture of three gases: hydrogen (H2), carbon monoxide (CO), and carbon dioxide (CO2). Syngas already is widely used as a non-fossil fuel and a building block for a variety of chemicals using the Fischer-Tropsch process. Recently, syngas fermentation has attracted attention as a more sustainable way for the conversion of syngas to chemicals, since its biocatalysts are self-generating, are resilient, and can utilize a wide range of syngas compositions. However, syngas fermentation has technical and economic limitations. This dissertation, by contributing to the understanding of syngas fermentation, helps to overcome the limitations. A bibliometric analysis showed the topic’s landscape and identified that mass transfer is the biggest challenge for the process. One means to improve syngas mass transfer is to use the membrane biofilm reactor, or MBfR, to deliver syngas to the microorganisms. MBfR experiments delivering pure H2 demonstrated that the H2:IC ratio (IC is inorganic carbon) controlled the overall production rate of organic compounds and their carbon-chain length. Organic chemicals up to eight carbons could be produced with a high H2:IC ratio. A novel asymmetric membrane dramatically improved mass transfer rates for all syngas components, and its low selectivity among them made it ideal for high-rate syngas fermentation. MBfR experiments using syngas and the asymmetric membrane, as well as a conventional symmetric membrane, confirmed that the key parameter for generating long-chain products was a high H2:IC ratio. The fast mass transfer rate of the asymmetric membrane allowed a very high areal production rate of acetate: 253 g.m-2.d-1, the highest reported to date. Since the membrane delivered H2 and C from the syngas feed, the relatively low selectivity of the asymmetric membrane favored acetogenesis over microbial chain elongation. A techno-economic analysis of the MBfR showed that the cost to produce acetate was less than its market price. All results presented in this dissertation support the potential of syngas fermentation using the MBfR as a means to produce commodity chemicals and biofuels from syngas.
ContributorsCalvo Martinez, Diana Carolina (Author) / Rittmann, Bruce E (Thesis advisor) / Torres, César I (Thesis advisor) / Kralmajnik-Brown, Rosa (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
Widespread use of halogenated organic compounds for commercial and industrial purposes makes halogenated organic pollutants (HOPs) a global challenge for environmental quality. Current wastewater treatment plants (WWTPs) are successful at reducing chemical oxygen demand (COD), but the removal of HOPs often is poor. Since HOPs are xenobiotics, the biodegradation of HOPs is usually limited in the WWTPs. The current methods for HOPs treatments (e.g., chemical, photochemical, electrochemical, and biological methods) do have their limitations for practical applications. Therefore, a combination of catalytic and biological treatment methods may overcome the challenges of HOPs removal.This dissertation investigated a novel catalytic and biological synergistic platform to treat HOPs. 4-chlorophenol (4-CP) and halogenated herbicides were used as model pollutants for the HOPs removal tests. The biological part of experiments documented successful co-oxidation of HOPs and analog non-halogenated organic pollutants (OPs) (as the primary substrates) in the continuous operation of O2-based membrane biofilm reactor (O2-MBfR). In the first stage of the synergistic platform, HOPs were reductively dehalogenated to less toxic and more biodegradable OPs during continuous operation of a H2-based membrane catalytic-film reactor (H2-MCfR). The synergistic platform experiments demonstrated that OPs generated in the H2-MCfR were used as the primary substrates to support the co-oxidation of HOPs in the subsequent O2-MBfR. Once at least 90% conversation of HOPs to OPs was achieved in the H2-MCfR, the products (OPs to HOPs mole ratio >9) in the effluent could be completely mineralized through co-oxidation in O2-MBfR. By using H2 gas as the primary substrate, instead adding the analog OP, the synergistic platform greatly reduced chemical costs and carbon-dioxide emissions during HOPs co-oxidation.
ContributorsLuo, Yihao (Author) / Rittmann, Bruce (Thesis advisor) / Krajmalnik-Brown, Rosa (Committee member) / Torres, Cesar (Committee member) / Arizona State University (Publisher)
Created2022
Description
Energy can be harvested from wastewater using microbial fuel cells (MFC). In order to increase power generation, MFCs can be scaled-up. The MFCs are designed with two air cathodes and two anode electrodes. The limiting electrode for power generation is the cathode and in order to maximize power, the cathodes were made out of a C-N-Fe catalyst and a polytetrafluoroethylene binder which had a higher current production at -3.2 mA/cm2 than previous carbon felt cathodes at -0.15 mA/cm2 at a potential of -0.29 V. Commercial microbial fuel cells from Aquacycl were tested for their power production while operating with simulated blackwater achieved an average of 5.67 mW per cell. The small MFC with the C-N-Fe catalyst and one cathode was able to generate 8.7 mW. Imitating the Aquacycl cells, the new MFC was a scaled-up version of the small MFC where the cathode surface area increased from 81 cm2 to 200 cm2. While the MFC was operating with simulated blackwater, the peak power produced was 14.8 mW, more than the smaller MFC, but only increasing in the scaled-up MFC by 1.7 when the surface area of the cathode increased by 2.46. Further long-term application can be done, as well as operating multiple MFCs in series to generate more power and improve the design.
ContributorsRussell, Andrea (Author) / Torres, Cesar (Thesis advisor) / Garcia Segura, Sergio (Committee member) / Fraser, Matthew (Committee member) / Arizona State University (Publisher)
Created2022
Description
Groundwater contamination is of environmental and human health concern. Bioremediation is a nature-based method for contaminant treatment. Bioremediation, which relies on the ability of microorganisms to destroy or transform contaminants, must be reliable and cost-competitive in comparison to more traditional treatment methods. Two hurdles must be overcome to enhance bioremediation’s effectiveness and competitiveness: i) being able to degrade recalcitrant compounds, and ii) being able to control the growth rate and location of microorganisms involved in bioremediation in the subsurface. My dissertation adds foundational knowledge and engineering application on how to biodegrade recalcitrant emerging and legacy halogenated compounds. Generating biotransformation knowledge on the recalcitrant emerging contaminants called per- and polyfluoroalkyl substances (PFAS) may lead to solutions for protecting both people and the planet. In my dissertation, I analyzed PFAS biotransformation and microbial defluorination literature via meta-analytical and bibliometric methods to identify unexplored topics and experimental conditions. The metanalytical work identified trends in PFAS microbial biotransformation science to inform future experimental design.
The second hurdle which must be overcome is being able to control bacterial growth in the subsurface. During bioremediation implementation microbial overgrowth may clog injection wells and the subsurface, leading to reduced porosity and treatment efficacy. Contaminant treatment schemes based on aerobic cometabolism frequently exhibit overgrowth at subsurface injection points for O2 (the electron acceptor) and a labile hydrocarbon (e.g., propane). My dissertation work experimentally evaluated acetylene as a microbial inhibitor for use in controlling microbial overgrowth during trichloroethene (TCE) aerobic cometabolism. I demonstrated that acetylene reduces the likelihood of microbial overgrowth of TCE-degrading microorganisms in soil-free microcosms and aquifer soil columns while retaining TCE degradation capacity. Cumulatively, my dissertation provides foundational knowledge for academics and bioremediation practitioners to develop robust and reliable bioremediation technologies.
ContributorsSkinner, Justin Paul (Author) / Delgado, Anca G. (Thesis advisor) / Rittmann, Bruce E (Committee member) / Chu, Min Ying Jacob (Committee member) / Arizona State University (Publisher)
Created2023