Many studies have demonstrated that there is a strong relationship between endothelial dysfunction and oxidative stress and have demonstrated also that hyperglycemia is associated with increased generation of oxidative stress and atherosclerotic vascular diseases, but we do not know how hydrogen peroxide (H2O2) and high glucose (HG) could affect calcium regulatory proteins of human vascular endothelial cells (HUVECs) in vitro. In the present study, we have examined the acute effect of H2O2 (100 M) and the effect of chronic exposure to HG concentration (35 mM) on the calcium regulatory system of human vascular endothelial cells using fluorescence imaging microscopy (fura-2). In this study, we tested the hypothesis that calcium regulatory proteins (SERCA-ATPase and PMCA-ATPase pumps and the NCX exchanger) of ECs have different sensitivities to H2O2 and high glucose concentration. We also tested the hypothesis that calcium regulatory proteins could be potential targets of ROS at the early stage of vascular disease. The results of this study showed that both H2O2 and high glucose induced significant delay in calcium removal time (CRT). The study of H2O2 showed that the delay in CRT was due to partial inhibition of SERCA-ATPase and the sodium calcium exchanger (NCX) activity and the effect of H2O2 on CRT was reversible. In contrast, the PMCA-ATPase pump was resistant to inhibition by H2O2. Furthermore, H2O2 induced a 40 ± 6.5 % reduction in endoplasmic reticulum refilling. The second part of the study showed that exposure of ECs to HG concentration for 10 days induced a significant delay in CRT and this delay was due to partial blockade of the SERCA-ATPase pump. Blockade of PMCA-ATPase pump with vanadate showed a further delay in CRT. We conclude that: 1- Both H2O2 and HG affected components of the calcium removal system with different sensitivities; 2- H2O2 and HG did not show any inhibitory effects on the PMCA-ATPase pump; 3- The effect of H2O2 on CRT was reversible; 4- The effect of HG on CRT could be due to increased production of H2O2; 5- The calcium regulatory proteins of ECs could be potential targets for ROS during the early stage of a cardio-vascular disease such as diabetes mellitus.

In situ chemical oxidation (ISCO) is a leading-edge technology for soil and groundwater remediation, and involves injecting a chemical oxidant (e. g. , permanganate, hydrogen peroxide, or persulfate) into the subsurface to deplete contaminant mass through oxidation. Since the delivery of the chosen oxidant to the target treatment zone must occur in situ, the interaction between the injected oxidant and the aquifer material is a key controlling factor for a successful ISCO application. While many published ISCO studies have focused on the interaction between an oxidant and target contaminants, many questions still remain on the interaction between a potential oxidant and the aquifer material. Through a series of bench-scale experiments with aquifer materials collected from 10 sites throughout North America, the research presented in this thesis provides insight into the interaction between these aquifer materials and two widely used ISCO oxidants; permanganate and hydrogen peroxide. <br /><br /> The investigation into the interaction between aquifer materials and permanganate consisted of three series of bench-scale experiments: (1) long-term batch experiments which were used to investigate permanganate consumption in response to fundamental geochemical properties of the aquifer materials, (2) short-term batch experiments which were designed to yield kinetic data that describe the behavior of permanganate in the presence of various aquifer materials, and (3) column experiments which were used to investigate permanganate transport in a system that mimics the subsurface environment. The long-term experiments which involved more than 180 batch reactors monitored for ~300 days showed that the unproductive permanganate consumption by aquifer materials or natural oxidant demand (NOD) is strongly affected by the initial permanganate concentration, permanganate to solid mass ratio, and the reductive components associated with each aquifer material. This consumption cannot be represented by an instantaneous reaction process but is kinetically controlled by at least a fast and slow reactive component. Accordingly, an empirical expression for permanganate NOD in terms of aquifer material properties, and a hypothetical kinetic model consisting of two reaction components were developed. In addition, a fast and economical permanganate NOD estimation procedure based on a permanganate COD test was developed and tested. The investigation into short-term permanganate consumption (time scale of hours) was based on the theoretical derivation of the stoichiometric reaction of permanganate with bulk aquifer material reductive components, and consisted of excess permanganate mass experiments and excess aquifer material mass experiments. The results demonstrated that permanganate consumption by aquifer materials can be characterized by a very fast reaction on the order of minutes to hours, confirming the existence of the fast reaction component of the hypothetical kinetic model used to describe the long-term permanganate NOD observations. A typical experimental column trial consisted of flushing an aquifer-material packed column with the permanganate source solution until sufficient permanganate breakthrough was observed. The permanganate column results indicated the presence of a fast and slow consumption rate consistent with the long-term batch test data, and an intermediate consumption rate affecting the shape of the rising limb of the breakthrough curve. Finally, a comparison of the experimental results between batch and column systems indicated that permanganate NOD was significantly overestimated by the batch experiments; however, permanganate consumption displayed some similarity between the batch and column systems and hence an empirical expression was developed to predict permanganate consumption in physically representative column systems from batch reactor data. <br /><br /> The interaction between hydrogen peroxide and aquifer materials was also investigated with both batch and column experiments. A series of batch experiments consisting of a mixture of 2% hydrogen peroxide and 15 g of aquifer materials was used to capture the overall hydrogen peroxide behavior in the presence of various aquifer materials. The results indicated that the decomposition of hydrogen peroxide in the presence of various aquifer materials followed a first-order rate law, and was strongly affected by the content of amorphous transition metals (i. e. , Fe and Mn). Although hydrogen peroxide decomposition is related to the total organic carbon (TOC) content of natural aquifer materials, the results from a two-week long exposure to hydrogen peroxide suggests that not all forms of natural organic matter contributed to this decomposition. A multiple linear regression analysis was used to generate predictive relationships to estimate hydrogen peroxide decomposition rate coefficients based on various aquifer material properties. The enhanced stability of hydrogen peroxide was investigated under six scenarios with the addition of chelating reagents. The impact of a new green chelating reagent, S,S'-ethylenediaminedisuccinate (EDDS), on the stability of hydrogen peroxide in the presence of aquifer materials was experimentally examined and compared to that of the traditional and widely used chelating reagent, Ethylenediaminetetraacetic (EDTA). The results demonstrated that EDDS was able to significantly increase the stability of hydrogen peroxide, especially for aquifer materials with low TOC contents and/or high dissolvable Fe and Mn contents. Finally, to complement and expand the findings from the batch experiments, column experiments were conducted with aquifer materials from five representative sites. Each column was flushed with two types of source solutions (with or without EDDS addition) at two flow rates. The column experiments showed that the use of EDDS resulted in an earlier breakthrough and a higher stable concentration of hydrogen peroxide relative to the case without the addition of EDDS. The hydrogen peroxide decomposition rate coefficients generated from the column data were significantly higher than those generated from the batch test data and no correlation between hydrogen peroxide decomposition coefficients obtained from column and batch experiments was observed. Based on the column experimental results, a one-dimensional transport model was also calibrated to capture the hydrogen peroxide breakthrough process. <br /><br /> Data from bench-scale tests are routinely used to support both ISCO design and site screening, and therefore the findings from this study can be used as guidance on the utility of these tests to generate reliable and useful information. In general, the behavior of both permanganate and hydrogen peroxide in the presence of aquifer materials in batch and the column systems clearly indicates that the use of batch test data for ISCO system design is questionable since column experiments are believed to mimic in situ conditions better since column systems provide more realistic aquifer material contact. Thus the scaling relationships developed in this study provide meaningful tools to transfer information obtained from batch systems, which are widely employed in most bench-scale studies, to column systems.

In situ chemical oxidation (ISCO) is a leading-edge technology for soil and groundwater remediation, and involves injecting a chemical oxidant (e. g. , permanganate, hydrogen peroxide, or persulfate) into the subsurface to deplete contaminant mass through oxidation. Since the delivery of the chosen oxidant to the target treatment zone must occur in situ, the interaction between the injected oxidant and the aquifer material is a key controlling factor for a successful ISCO application. While many published ISCO studies have focused on the interaction between an oxidant and target contaminants, many questions still remain on the interaction between a potential oxidant and the aquifer material. Through a series of bench-scale experiments with aquifer materials collected from 10 sites throughout North America, the research presented in this thesis provides insight into the interaction between these aquifer materials and two widely used ISCO oxidants; permanganate and hydrogen peroxide. <br /><br /> The investigation into the interaction between aquifer materials and permanganate consisted of three series of bench-scale experiments: (1) long-term batch experiments which were used to investigate permanganate consumption in response to fundamental geochemical properties of the aquifer materials, (2) short-term batch experiments which were designed to yield kinetic data that describe the behavior of permanganate in the presence of various aquifer materials, and (3) column experiments which were used to investigate permanganate transport in a system that mimics the subsurface environment. The long-term experiments which involved more than 180 batch reactors monitored for ~300 days showed that the unproductive permanganate consumption by aquifer materials or natural oxidant demand (NOD) is strongly affected by the initial permanganate concentration, permanganate to solid mass ratio, and the reductive components associated with each aquifer material. This consumption cannot be represented by an instantaneous reaction process but is kinetically controlled by at least a fast and slow reactive component. Accordingly, an empirical expression for permanganate NOD in terms of aquifer material properties, and a hypothetical kinetic model consisting of two reaction components were developed. In addition, a fast and economical permanganate NOD estimation procedure based on a permanganate COD test was developed and tested. The investigation into short-term permanganate consumption (time scale of hours) was based on the theoretical derivation of the stoichiometric reaction of permanganate with bulk aquifer material reductive components, and consisted of excess permanganate mass experiments and excess aquifer material mass experiments. The results demonstrated that permanganate consumption by aquifer materials can be characterized by a very fast reaction on the order of minutes to hours, confirming the existence of the fast reaction component of the hypothetical kinetic model used to describe the long-term permanganate NOD observations. A typical experimental column trial consisted of flushing an aquifer-material packed column with the permanganate source solution until sufficient permanganate breakthrough was observed. The permanganate column results indicated the presence of a fast and slow consumption rate consistent with the long-term batch test data, and an intermediate consumption rate affecting the shape of the rising limb of the breakthrough curve. Finally, a comparison of the experimental results between batch and column systems indicated that permanganate NOD was significantly overestimated by the batch experiments; however, permanganate consumption displayed some similarity between the batch and column systems and hence an empirical expression was developed to predict permanganate consumption in physically representative column systems from batch reactor data. <br /><br /> The interaction between hydrogen peroxide and aquifer materials was also investigated with both batch and column experiments. A series of batch experiments consisting of a mixture of 2% hydrogen peroxide and 15 g of aquifer materials was used to capture the overall hydrogen peroxide behavior in the presence of various aquifer materials. The results indicated that the decomposition of hydrogen peroxide in the presence of various aquifer materials followed a first-order rate law, and was strongly affected by the content of amorphous transition metals (i. e. , Fe and Mn). Although hydrogen peroxide decomposition is related to the total organic carbon (TOC) content of natural aquifer materials, the results from a two-week long exposure to hydrogen peroxide suggests that not all forms of natural organic matter contributed to this decomposition. A multiple linear regression analysis was used to generate predictive relationships to estimate hydrogen peroxide decomposition rate coefficients based on various aquifer material properties. The enhanced stability of hydrogen peroxide was investigated under six scenarios with the addition of chelating reagents. The impact of a new green chelating reagent, S,S'-ethylenediaminedisuccinate (EDDS), on the stability of hydrogen peroxide in the presence of aquifer materials was experimentally examined and compared to that of the traditional and widely used chelating reagent, Ethylenediaminetetraacetic (EDTA). The results demonstrated that EDDS was able to significantly increase the stability of hydrogen peroxide, especially for aquifer materials with low TOC contents and/or high dissolvable Fe and Mn contents. Finally, to complement and expand the findings from the batch experiments, column experiments were conducted with aquifer materials from five representative sites. Each column was flushed with two types of source solutions (with or without EDDS addition) at two flow rates. The column experiments showed that the use of EDDS resulted in an earlier breakthrough and a higher stable concentration of hydrogen peroxide relative to the case without the addition of EDDS. The hydrogen peroxide decomposition rate coefficients generated from the column data were significantly higher than those generated from the batch test data and no correlation between hydrogen peroxide decomposition coefficients obtained from column and batch experiments was observed. Based on the column experimental results, a one-dimensional transport model was also calibrated to capture the hydrogen peroxide breakthrough process. <br /><br /> Data from bench-scale tests are routinely used to support both ISCO design and site screening, and therefore the findings from this study can be used as guidance on the utility of these tests to generate reliable and useful information. In general, the behavior of both permanganate and hydrogen peroxide in the presence of aquifer materials in batch and the column systems clearly indicates that the use of batch test data for ISCO system design is questionable since column experiments are believed to mimic in situ conditions better since column systems provide more realistic aquifer material contact. Thus the scaling relationships developed in this study provide meaningful tools to transfer information obtained from batch systems, which are widely employed in most bench-scale studies, to column systems.

<i>In vivo</i> and <i>in vitro</i> studies on numerous types of blood vessels obtained from a variety of vascular beds and species have demonstrated that oxygen free radicals (OFRs) can evoke both vasodilation and vasoconstriction. Specific OFRs have been shown to elicit different and often times opposite effects on vascular smooth muscle. Therefore, this thesis attempts to define the vascular actions and mechanism of oxygen free radicals (OFRs) [superoxide anion (O₂^-), hydrogen peroxide (HO₂) and hydroxyl radical (OH)] on isolated rabbit aorta. This thesis will examine the role of OH in Ach- and nitroglycerin (NTG)-induced relaxation of isolated rabbit aorta. Superoxide anions generated by xanthine (X) plus xanthine oxidase (XO) produced concentration-dependent contractions of isolated rabbit aorta. The contractile response to O₂^- was completely abolished in preparations denuded of endothellum or pretreated with superoxide dismutase (SOD), a scavenger of O₂^-. The contractile response was reduced by indomethacin (I), a cyclooxygenase inhibitor. These results suggest that O₂^- mediated by vasoconstrictor arachidonic acid metabolites. Hydrogen peroxide generated by glucose and glucose oxidase produced contraction (low concentrations) and relaxation followed by contraction (high concentrations) in isolated rabbit aorta. The contractile response was abolished in the presence of catalase, a scavenger of H₂O₂ however the relaxant effect was exaggerated. Indomethacin markedly reduced the H₂O₂-induced contraction. Relaxation was completely prevented by de-endothelialization or pretreatment with N^G-monomethyl-L-arginine (LNMMA), an inhibitor of nitric oxide synthetase. These results suggest that H₂O₂ in large concentrations produces a biphasic response, relaxation followed by contraction. Relaxation is endothelium dependent and is mediated by endothelium-derived relaxing factor (EDRF), nitric oxide (NO). The contractile response is endothelium independent and is mediated by vasoconstrictor arachidonic acid metabolites of smooth muscle. Hydroxyl radicals generated by dihydroxyfumarate (DHF), ferric chloride (FeCl₃) and adenosine diphosphate (ADP) (DHF/FeCl₃-ADP) produced concentration dependent relaxations of NE-precontracted rabbit aorta. Mannitol (Ml) completely inhibited OH-induced relaxation. Relaxation was markedly reduced in aortic rings mechanically denuded of endothelium. The relaxant effect was reduced by an inhibitor of NO synthesis (LNMMA), by an inhibitor of guanylate cyclase (methylene blue), by an inhibitor of cyclooxygenase (indomethacin) and by an inhibitor of an ATP-sensitive K⁺ channel blocker (glyburide). These results indicate that OH produces relaxation that is endothelium-dependent and partially mediated by an endothelium-derived relaxing factor (NO), vasodilatory arachidonic acid metabolites and an ATP-sensitive K⁺ channel. We hypothesized that Ach-induced vascular relaxation is mediated by OH derived from the interaction of NO and O₂^-. To test this hypothesis we investigated the effect of Ach and NTG on NE-precontracted isolated rabbit aortic preparations in the absence or presence of scavengers of O₂^- (SOD), and OH (dimethylthiourea (DMTU) or mannitol or Garlicin). The OFR scavengers (SOD, dimethylthiourea, mannitol, garlicin and histidine) alone or the combination of SOD and DMTU markedly reduced Ach- or NTG-induced relaxation. However, the combination of histidine, (a ¹O₂ scavenger) SOD and DMTU completely abolished Ach-induced relaxation.

Monoamine oxidase (MAO) is a mitochondrial deaminating enzyme that exists as two isoforms, MAO-A and -B. The MAO-mediated reaction generates hydrogen peroxide (H2O2) as a normal by-product. Dysregulation of MAO has been implicated in a variety of neuropsychiatric and neurodegenerative disorders, as well as in the aging process. Endogenous regulators of MAO-A function include calcium (Ca2+) and the p38 mitogen-activated protein kinase (MAPK). Although the effect of p38(MAPK) is thought to rely on induction of mao-A gene expression, post-translational modification of the MAO-A protein is also possible. <p>Using standard biochemical approaches in combination with pharmacological interventions and recombinant DNA strategies, specific aspartic acid residues (within putative Ca2+-binding motifs) were demonstrated to contribute to MAO-A activity. Furthermore, MAO-A activity and its sensitivity to Ca2+ was negatively regulated by the p38(MAPK), which is usually activated during cell stress. The effect of p38(MAPK) on MAO-A function relies specifically on Serine209 in MAO-A, which resides in a p38(MAPK) consensus motif. The serine phosphorylation status of MAO-A determines its capacity for generating peroxy radicals and its toxicity in established cell lines (e.g. C6, N2a, HEK293A, HT-22) and in primary cortical neurons. p38(MAPK)-regulated MAO-A activity is also linked to neurotoxicity associated with the Alzheimer disease-related peptide, Ò-amyloid (AÒ). These data suggest a unique neuroprotective role for p38(MAPK) centered on a negative feedback regulation of the Ca2+-sensitive, H2O2-generating enzyme MAO-A.

This current study is a lab-scale investigation focused on the treatment of stormwater runoff generated in wood-storage areas. The main target constituents of the proposed treatment were: metals (Cu, Cd, Co, V, Pb, Zn, Ni, Cr, Fe, As), COD, TOC, Phenols, and color. The method implemented for this project follows the main concept of using low-cost and environmentally friendly technologies and had as main steps the use of a by-product of wood-based industries - wood fly ashes as sorbents - followed by oxidation with H2O2 (Hydrogen Peroxide). The results obtained during this investigation were vey promising since satisfactory removal % was achieved. Removal rates of 98.5%, 86%, 89.6%, 79.6% were achieved for color, chemical oxygen demand (COD), total organic carbon (TOC) and phenols respectively. Furthermore a decrease in metals concentrations was also observed with the exception of chromium. The study showed that for 300 ml storm water, optimum conditions were with 7g wood fly ash, 5 hours time reaction, pH≈11.46 and 150 μl of a 30% H2O2 solution in a room temperature. To conclude it can be stated that the use of a by-product from wood industry to treat contaminated water from the same sector, following the concept of a closed-loop system, is promising and possible. However further studies need to be conducted in order to evaluate such system in scaled-up conditions.

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Hepatocellular carcinoma (HCC) is one of the most common and devastating malignant tumors in Taiwan. Due to an imbalanced between reactive oxygen species (ROS) production and detoxification, oxidative stress, has been implicated in liver carcinogenesis. Superoxide dismutases (SODS) play a key role in the detoxification of superoxide radicals and thus protect cells from damage induced by free radicals. Manganese superoxide dismutase (MnSOD or SOD2) is a member of the superoxide dismutase family located in mitochondria. SOD2 transforms toxic superoxide, a byproduct of the mitochondrial electron transport chain, into hydrogen peroxide and diatomic oxygen. Though reduced SOD2 protein level and activities have been reported in hepatoma tissues, it remains unclear how SOD2 expression affected the tumorigenic processes of hepatoma cells. Expression analysis of an array of human HCC cell lines revealed that SOD2 were down-regulated in poorly differentiated SK-Hep-1 hepatoma cells. Moreover, SOD2 is downregulated in 68.8% of resected HCC samples (97 out of 141 cases). Adenovirus-mediated SOD2 gene delivery increased the cellular SOD2 protein level and H2O2 production, but reduced the superoxide anion level in SK-Hep-1 cells. Furthermore, SOD2 restoration significantly reduced the proliferation, motility, and colony formation of SK-Hep-1 cells. In vivo animal model, the finding of SOD2 overexpression inhibited the proliferation of Sk-Hep-1 hepatoma cells while reduced the tumor growth in mice. Flow cytometry analysis showed that SOD2 gene transfer inhibited the growth of hepatoma cells through induction of cell cycle arrest at G2/M phase. This was associated with declined cdc2/cdk1 and cyclin B1 expression and upregulation p21Cip1 by SOD2 gene delivery. However, SOD2 overexpression had no effect on the secretion of matrix metalloproteinase-2 (MMP-2) and MMP-9.In conclusion, SOD2 overexpression suppresses the tumorigenicity of hepatoma cells and may hold promise for HCC treatment.