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Cyanobacteria and microalgae help reduce the environmental impact of human energy consumption by playing a vital role in carbon and nitrogen cycling. They are also used in various applications like biofuel production, food, medicine, and bioremediation. Understanding how these organisms respond to stress is important for efficient recovery strategies and

Cyanobacteria and microalgae help reduce the environmental impact of human energy consumption by playing a vital role in carbon and nitrogen cycling. They are also used in various applications like biofuel production, food, medicine, and bioremediation. Understanding how these organisms respond to stress is important for efficient recovery strategies and sustainable outcomes. This study investigated the effects of low-level bleaching and thermal stress on cyanobacteria and microalgae, specifically Synechocystis, Chlorella, and Scenedesmus. The role of ferroptosis, an iron-dependent form of cell death, in the degradation of cellular components under these stressors was examined. Flow cytometry and spectrophotometry were used to measure changes in cellular health and viability. The results showed that temperature influences the type of cell death mechanism and can impact photosynthetic organisms. When treated with Liproxstatin-1, an inhibitor of ferroptosis, both Synechocystis and Chlorella experienced a decrease in oxidative damage, suggesting a potential protective role for the compound. Further investigation into ferroptosis and other forms of cell death, as well as identifying additional inhibitory molecules, could lead to strategies for mitigating oxidative stress and enhancing the resilience of cyanobacteria and microalgae.

ContributorsRayes, Rammy (Author) / Rittmann, Bruce (Thesis director) / Eustance, Everett (Committee member) / Lewis, Christine (Committee member) / Khdour, Omar (Committee member) / Barrett, The Honors College (Contributor) / School of Life Sciences (Contributor)
Created2023-05
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Description
Population growth and fresh water depletion challenge drinking water utilities. Surface water quality is impacted significantly by climate variability, human activities, and extreme events like natural disasters. Dissolved organic carbon (DOC) is an important water quality index and the precursor of disinfection by-products (DBPs) that varies with both hydrologic and

Population growth and fresh water depletion challenge drinking water utilities. Surface water quality is impacted significantly by climate variability, human activities, and extreme events like natural disasters. Dissolved organic carbon (DOC) is an important water quality index and the precursor of disinfection by-products (DBPs) that varies with both hydrologic and anthropogenic factors. Granular activated carbon (GAC) is a best available technology for utilities to meet Stage 2 D/DBP rule compliance and to remove contaminants of emerging concern (CECs) (e.g., pharmaceutical, personal care products (PCPs), etc.). Utilities can operate GAC with more efficient and flexible strategies with the understanding of organic occurrence in source water and a model capable predicting DOC occurrence. In this dissertation, it was found that DOC loading significantly correlated with spring runoff and was intensified by dry-duration antecedent to first flush. Dynamic modeling based on reservoir management (e.g., pump-back operation) was established to simulate the DOC transport in the reservoir system. Additionally, summer water recreational activities were found to raise the level of PCPs, especially skin-applied products, in raw waters. GAC was examined in this dissertation for both carbonaceous and emerging nitrogenous DBP (N-DBP) precursors (i.e., dissolved organic nitrogen (DON)) removal. Based on the experimental findings, GAC preferentially removes UV254-absorbing material, and DOC is preferentially removed over DON which may be composed primarily of hydrophilic organic and results in the low affinity for adsorption by GAC. The presence of organic nitrogen can elevate the toxicity of DBPs by forming N-DBPs, and this could be a major drawback for facilities considering installation of a GAC adsorber owing to the poor removal efficiency of DON by GAC. A modeling approach was established for predicting DOC and DON breakthrough during GAC operation. However, installation of GAC adsorber is a burden for utilities with respect to operational and maintenance cost. It is common for utilities to regenerate saturated GAC in order to save the cost of purchasing fresh GAC. The traditional thermal regeneration technology for saturated GAC is an energy intensive process requiring high temperature of incineration. Additionally, small water treatment sites usually ship saturated GAC to specialized facilities for regeneration increasing the already significant carbon footprint of thermal regeneration. An innovative GAC regeneration technique was investigated in this dissertation for the feasibility as on-site water treatment process. Virgin GAC was first saturated by organic contaminant then regenerated in-situ by iron oxide nanocatalysts mixed with hydrogen peroxide. At least 70 % of adsorption capacity of GAC can be regenerated repeatedly for experiments using modeling compound (phenol) or natural organic matter (Suwannee River humic acid). The regeneration efficiency increases with increasing adsorbate concentration. Used-iron nanocatalysts can be recovered repeatedly without significant loss of catalytic ability. This in-situ regeneration technique provides cost and energy efficient solution for water utilities considering GAC installation. Overall, patterns were found for DOC and CEC variations in drinking water sources. Increasing concentrations of bulk (DOC and DON) and/or trace organics challenge GAC operation in utilities that have limited numbers of bed-volume treated before regeneration is required. In-situ regeneration using iron nanocatalysts and hydrogen peroxide provides utilities an alternative energy-efficient operation mode when considering installation of GAC adsorber.
ContributorsChiu, Chao-An (Author) / Westerhoff, Paul (Thesis advisor) / Rittmann, Bruce (Committee member) / Hristovski, Kiril (Committee member) / Arizona State University (Publisher)
Created2012
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Description
The need for clean fuel sources is greater than ever, as fossil fuel dependence has soared and harmful emissions are being released into the atmosphere at increasingly higher rates. A viable solution to this issue is the use of microalgae for the creation of biofuels, as it holds a high

The need for clean fuel sources is greater than ever, as fossil fuel dependence has soared and harmful emissions are being released into the atmosphere at increasingly higher rates. A viable solution to this issue is the use of microalgae for the creation of biofuels, as it holds a high concentration of lipids without requiring arable land for growth. This experiment studies downstream applications of microalgae, including how the extraction efficiency can be improved for greater lipid yield. 3-dimethyldodecylammonium propanesulfonate, myristyltrimethylammonium bromide and sodium dodecyl sulfate were used as surfactants to break down the algae cell walls and improve lipid recovery. The incubation times of the biomass in the surfactant were also studied at 0, 4.5, 24, 48 and 72 hours to more fully examine how surfactants affect the extraction of lipids. Along with this, hexane and isopropanol were used as the main extraction solvent in this experiment, but testing was done to compare these lipid yields to when ethyl acetate was used as the solvent. It was found that the MTMAB surfactant led to the greatest cell disruption, as its lipid yields were consistently higher than those of the other surfactants. Also, longer incubation times did improve the amount of lipid extracted, showing that the surfactants do have a strong effect on the cell breakdown. Finally, it was found that the ethyl acetate was a slightly more effective solvent than hexane and isopropanol in the conditions of this experiment. Overall, a stronger understanding of the wet extraction process was gained from these tests, as well as more insight into how some of the variables interact and work together during extraction.
ContributorsMartarella, Rebecca Lynne (Author) / Rittmann, Bruce (Thesis director) / Lai, Sean Yen-Jung (Committee member) / Chemical Engineering Program (Contributor) / Barrett, The Honors College (Contributor)
Created2015-12
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Description

In order for microalgae to be a cost-effective renewable energy source, a high CO2-transfer efficiency (CTE) is necessary. Using hollow-fiber membranes (HFM), membrane carbonation (MC) in microalgal cultivation can be used to achieve a CTE near 100%. Due to the diurnal cycle in outdoor algal cultivation, an inconsistent CO2 demand

In order for microalgae to be a cost-effective renewable energy source, a high CO2-transfer efficiency (CTE) is necessary. Using hollow-fiber membranes (HFM), membrane carbonation (MC) in microalgal cultivation can be used to achieve a CTE near 100%. Due to the diurnal cycle in outdoor algal cultivation, an inconsistent CO2 demand with temperature fluctuations can cause pore wetting of the inner and outer fiber layers in composite HFMs. In addition, the presence of supersaturated O2 during high algal growth may change the gas transfer dynamics of the fibers, which can be critical when trying to selectively remove CO2 from a valuable gas such as biogas. This study evaluated fiber performance under conditions that mimic these effects by analyzing the carbon transfer efficiency (CTE), CO2 flux (JCO2), and outlet CO2 concentration compared to baseline values. Wetting of the interior fiber macropores resulted in an average 32% ± 8.3% decrease in flux, which was greater than for flooding of the outer macropores, which showed no significant change. All tests resulted in a decrease in CTE and an increase in outlet CO2. The presence of elevated O2 levels did not decrease the CO2 flux compared to baseline values, but it increased the O2 concentration and decreased the CH4 concentration at the distal end of the fibers. These findings highlight that liquid accumulation can decrease HFM performance during MC for microalgal cultivation, while the presence of supersaturated O2 can reduce separation efficiency.

ContributorsFrias, Zoe (Author) / Rittmann, Bruce (Thesis director) / Eustance, Everett (Committee member) / Barrett, The Honors College (Contributor) / School of Molecular Sciences (Contributor) / School of Life Sciences (Contributor)
Created2021-12