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Microbial fuel cells (MFCs) promote the sustainable conversion of organic matter in black water to electrical current, enabling the production of hydrogen peroxide (H2O2) while making waste water treatment energy neutral or positive. H2O2 is useful in remote locations such as U.S. military forward operating bases (FOBs) for on-site tertiary

Microbial fuel cells (MFCs) promote the sustainable conversion of organic matter in black water to electrical current, enabling the production of hydrogen peroxide (H2O2) while making waste water treatment energy neutral or positive. H2O2 is useful in remote locations such as U.S. military forward operating bases (FOBs) for on-site tertiary water treatment or as a medical disinfectant, among many other uses. Various carbon-based catalysts and binders for use at the cathode of a an MFC for H2O2 production are explored using linear sweep voltammetry (LSV) and rotating ring-disk electrode (RRDE) techniques. The oxygen reduction reaction (ORR) at the cathode has slow kinetics at conditions present in the MFC, making it important to find a catalyst type and loading which promote a 2e- (rather than 4e-) reaction to maximize H2O2 formation. Using LSV methods, I compared the cathodic overpotentials associated with graphite and Vulcan carbon catalysts as well as Nafion and AS-4 binders. Vulcan carbon catalyst with Nafion binder produced the lowest overpotentials of any binder/catalyst combinations. Additionally, I determined that pH control may be required at the cathode due to large potential losses caused by hydroxide (OH-) concentration gradients. Furthermore, RRDE tests indicate that Vulcan carbon catalyst with a Nafion binder has a higher H2O2 production efficiency at lower catalyst loadings, but the trade-off is a greater potential loss due to higher activation energy. Therefore, an intermediate catalyst loading of 0.5 mg/cm2 Vulcan carbon with Nafion binder is recommended for the final MFC design. The chosen catalyst, binder, and loading will maximize H2O2 production, optimize MFC performance, and minimize the need for additional energy input into the system.
ContributorsStadie, Mikaela Johanna (Author) / Torres, Cesar (Thesis director) / Popat, Sudeep (Committee member) / Barrett, The Honors College (Contributor) / Chemical Engineering Program (Contributor)
Created2015-05
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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.

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
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Description
Anaerobic digestion (AD), a common process in wastewater treatment plants, is traditionally assessed with Biochemical Methane Potential (BMP) tests. Hydrolysis is considered its rate-limiting step. During my research, I assessed the impact of pretreatment on BMPs and microbial electrochemical cells (MECs). In the first set of experiments, BMP tests were

Anaerobic digestion (AD), a common process in wastewater treatment plants, is traditionally assessed with Biochemical Methane Potential (BMP) tests. Hydrolysis is considered its rate-limiting step. During my research, I assessed the impact of pretreatment on BMPs and microbial electrochemical cells (MECs). In the first set of experiments, BMP tests were performed using alkaline and thermal pretreated waste activated sludge (WAS), a control group, and a negative control group as samples and AD sludge (ADS) as inoculum. The data obtained suggested that BMPs do not necessarily require ADS, since samples without inoculum produced 5-20% more CH4. However, ADS appears to reduce the initial methanogenesis lag in BMPs, as no pH inhibition and immediate CH4 production were observed. Consumption rate constants, which are related to hydrolysis, were calculated using three methods based on CH4 production, SSCOD concentration, and the sum of both, called the lumped parameter. All the values observed were within literature values, yet each provide a different picture of what is happening in the system. For the second set of experiments, the current production of 3 H-type MECs were compared to the CH4 production of BMPs to assess WAS solids' biodegradability and consumption rates relative to the pretreatment methods employed for their substrate. BMPs fed with pretreated and control WAS solids were performed at 0.42 and 1.42 WAS-to-ADS ratios. An initial CH4 production lag of about 12 days was observed in the BMP assays, but MECs immediately began producing current. When compared in terms of COD, MECs produced more current than the BMPs produced CH4, indicating that the MEC may be capable of consuming different types of substrate and potentially overestimating CH4 production in anaerobic digesters. I also observed 2 to 3 different consumption events in MECs versus 3 for BMP assays, but these had similar magnitudes, durations, and starting times in the control and thermal pretreated WAS-fed assays and not in alkaline assays. This might indicate that MECs identified the differences of alkaline pretreatment, but not between control WAS and thermal pretreated WAS. Furthermore, HPLC results suggest at least one hydrolysis event, as valerate, butyrate, and traces of acetate are observed in the reactors' effluents. Moreover, a possible inhibition of valerate-fixing microbial communities due to pretreatment and the impossibility of valerate consumption by ARB might explain its presence in the reactors' effluents.
ContributorsBrown Munoz, Francisco (Author) / Torres, Cesar (Thesis director) / Rittmann, Bruce E. (Committee member) / Chemical Engineering Program (Contributor, Contributor) / Barrett, The Honors College (Contributor)
Created2017-05
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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

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
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Description
Exoelectrogenic microorganisms can grow by transferring electrons from their internal metabolism to extracellular substrates in a process known as extracellular electron transfer (EET). This dissertation explores the mechanisms of EET by both chemotrophic and phototrophic organisms and constructs a novel supramolecular structure that can be used as a model for

Exoelectrogenic microorganisms can grow by transferring electrons from their internal metabolism to extracellular substrates in a process known as extracellular electron transfer (EET). This dissertation explores the mechanisms of EET by both chemotrophic and phototrophic organisms and constructs a novel supramolecular structure that can be used as a model for microbial, long-range electron transfer. Geobacter sulfurreducens has been hypothesized to secrete and use riboflavin as a soluble, extracellular redox shuttle in conjunction with multi-heme, outer membrane, c-type cytochromes, but the required proteins and their properties have not been defined. To address the mechanism of extracellular electron transfer by G. sulfurreducens, the first part of this work explores the interaction between an outer membrane, octaheme, c-type cytochrome OmcZs from G. sulfurreducens and riboflavin. Interrogation via multiple physical techniques shows that OmcZs transfers electrons to riboflavin. By analogy to other characterized systems, riboflavin then likely interacts with extracellular acceptors directly. The second part of this work addresses the mechanisms of EET by the model cyanobacterium Synechocystis sp. PCC 6803. It has been hypothesized that Synechocystis employs conductive pili for production of extracellular current. However, the results herein show that a strain that does not have pili produces extracellular photocurrent in a direct electrochemical cell at a level similar to that by wild type cells. Furthermore, conductive atomic force microscopy (AFM) imaging is used to show that pili produced by the wild type organism are not conductive. Thus, an alternative EET mechanism must be operable. In the third part of this work, a supramolecular structure comprised of peptide and cytochromes designed to serve as a model for long-range electron transfer through cytochrome rich environments is described. The c-type cytochromes in this synthetic nanowire retain their redox activity after assembly and have suitable characteristics for long-range electron transfer. Taken together, the results of this dissertation not only inform on natural microbial mechanisms for EET but also provide a starting point to develop novel, synthetic systems.
ContributorsThirumurthy, Miyuki (Author) / Jones, Anne K (Thesis advisor) / Redding, Kevin (Committee member) / Torres, Cesar (Committee member) / Arizona State University (Publisher)
Created2019
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Description
The list of applications of plasmonic nanoparticles in the fields of energy research, sensing, and diagnostics and therapeutics is continuously growing. Processes for the synthesis of the nanoparticles for such applications should incorporate provision to easily functionalize the particle formed and should ideally not use toxic reagents or create toxic

The list of applications of plasmonic nanoparticles in the fields of energy research, sensing, and diagnostics and therapeutics is continuously growing. Processes for the synthesis of the nanoparticles for such applications should incorporate provision to easily functionalize the particle formed and should ideally not use toxic reagents or create toxic by-products. The traditional methods of synthesizing nanoparticles generally are energy inefficient, requires stringent conditions such as high temperature, pressure or extreme pH and often produces toxic by-products. Although there exist a few solution-based methods to solve this problem, there is one avenue which has recently gained attention for nanoparticle synthesis: using biomolecules to facilitate nanomaterials synthesis. Using biomolecules for synthesis can provide a template to guide the nucleation process and helps to keep conditions biocompatible while also combining the step of functionalization of the nanoparticle with its synthesis through the biomolecule itself. The dissertation focuses on studying the bio-templated synthesis of two such noble metal nanoparticle which have biomedical applications: gold and platinum. In chapter 2, Gold Nanoparticles (GNP), with long-term stability, were synthesized using Maltose Binding Protein (MBP) as templating agent. The site of gold interaction on MBP was identified by X-ray crystallography. A novel gold binding peptide, AT1 (YPFGGSGGSGM), was designed based on the orientation of the residues in the gold binding site, identified through crystallography. This designed peptide was also shown to have stabilized and affected the growth rate of GNP formation, in similar manner to MBP. Further in chapter 3, a nanosensor was formulated using a variation of this GNP-MBP system, to detect and measure ionizing radiation dose for cancer radiation therapy. Upon exposure to therapeutic levels of ionizing radiation, the MBP‐based sensor system formed gold nanoparticles with a dose‐dependent color that could be used to predict the amount of delivered X‐ray dose. In chapter 4, a similar system of protein templated synthesis was introduced for platinum nanoparticle (PtNP). Here, GroEL, a large homo-tetradecamer chaperone from E.coli, was used as templating and stabilizing agent for reduction of K2PtCl4 ions to form PtNP. To understand how GroEL interacts with the PtNPs and thereby stabilizes them, single-particle cryo-electron microscopy technique was used to model the complex in solution. A 3.8-Å resolution 3D cryo-EM map of GroEL depicting the location of PtNP inside its central cylindrical cavity was obtained. Fitting a GroEL model to the map revealed Arginine-268 from two adjacent subunits of GroEL interacting with the PtNP surface. Finally in chapter 5, a solution to the potential issues of single particle data processing on protein nanoparticle complexes, specifically with 2D classification, was developed by creating masking algorithms.
ContributorsThaker, Amar Nilkamal (Author) / Nannenga, Brent L (Thesis advisor) / Acharya, Abhinav (Committee member) / Torres, Cesar (Committee member) / Mills, Jeremy (Committee member) / Rege, Kaushal (Committee member) / Arizona State University (Publisher)
Created2020