Call number: LD2668 .T4 1985 S25 / Master of Science

ITC/USA 2009 Conference Proceedings / The Forty-Fifth Annual International Telemetering Conference and Technical Exhibition / October 26-29, 2009 / Riviera Hotel & Convention Center, Las Vegas, Nevada / In this project, a telemetry system is implemented to save firefighters from potential danger in their working environment. Each Firefighter has a "node" or "unit" attached to them which contains temperature, oxygen, and carbon-monoxide sensors, and a transceiver. Each node constantly transmits data collected by the sensors to a central "base station." The base station consists of a laptop which is monitored by the Fire Chief at a safe distance from the scene, and it displays gas levels. The base station monitors the sensor readings, and sets off an alarm locally and also at the node if a reading has reached a predetermined critical value.

Carbon monoxide (CO) is present in the troposphere as a product of fossil fuel combustion, biomass burning and the oxidation of volatile hydrocarbons. It is the principal sink of the hydroxyl radical (OH), thereby affecting the concentrations of greenhouse gases such as CH4 and O3. Consequently, CO has an atmospheric lifetime of 1-3 months, making it a good tracer for studying the long range transport of pollution. Satellite observations present a valuable tool to investigate tropospheric CO. The Atmospheric InfraRed Sounder (AIRS), onboard the Aqua satellite, is sensitive to tropospheric CO in ~50 of its 2378 channels. This sensitivity to CO, combined with the daily global coverage provided by AIRS, makes AIRS a potentially useful instrument for observing CO sources and transport. An optimal estimation retrieval scheme has been developed for AIRS, to provide CO profiles from near-surface altitudes to 150 hPa. Through a validation study, using CO profiles from in-situ aircraft measurements, this retrieval scheme has been shown to provide CO observations with strong correlations to in situ measurements. Compared to the operational AIRS v4 CO product this retrieval scheme is shown to provide total column CO retrievals with a reduced bias relative to the in situ measurements (~ -10% to ~ -1%). In addition, the optimal estimation retrieval is shown to provide improved estimation and characterization of the retrieval errors. Further validation work has been carried out through comparison with the established CO observations from the MOPITT instrument, onboard the Terra satellite. Good agreement (correlation coefficient > 0.9, and bias < 1.0 ppbv) between the instruments is observed in the mid-troposphere. At this level, the optimal estimation scheme is shown to remove a positive bias of ~10 ppbv, relative to MOPITT, that is present in the AIRS v4 CO product. The AIRS instrument is also shown to be less sensitive to CO in the lower troposphere than MOPITT. AIRS is also demonstrated to provide fewer pieces of independent information about the vertical structure of CO at tropical latitudes, where higher thermal contrast increases the sensitivity of MOPITT. Through time series analysis, the capability of AIRS to detect seasonal trends in CO is demonstrated. The potential of AIRS to be used to track, both horizontal and vertical, CO transport is explored. AIRS is shown to be capable of tracking horizontal transport, and to have potential to track vertical transport when combined with another satellite sensor.

We have recently demonstrated that heme oxygenase is expressed in both healing wounds and in pressure ulcers. Heme oxygenase has been shown to have important cytoprotective functions in myocardial ischemia-reperfusion injury and organ allograft survival. The cytoprotective effects of heme oxygenase are multifactorial. Besides reducing levels of pro-oxidant heme, heme oxygenase products (bilirubin, carbon monoxide, and iron) have been demonstrated to possess anti-oxidant, anti-inflammatory, anti-apoptotic, and anti-proliferative properties. These properties make heme oxygenase an attractive therapeutic target for the prevention and treatment of chronic wounds. The purpose of this study was two-fold: evaluate the effects of carbon monoxide (CO) on the expression of heme oxygenase (HO-1) in dermal fibroblasts, and determine and begin to investigate the mechanisms responsible for CO-induction of HO-1. The ability of a second-generation carbon monoxide donating molecule-tricarbonyldichlororuthenium (II) dimer (CORM-2) to induce HO-1 protein expression in dermal fibroblasts was examined. Western blotting techniques were utilized to determine HO-1 expression. CORM-2 (100-300uM) induced maximum expression of HO-1. The maximum response to CORM-2 occurred between 12 and 20 hours. Inhibition of MAPK, PI3-K, JNK pathways showed no changes in HO-1 expression. Likewise inhibition of cGMP, a known pathway for CO, had no effect on protein expression suggesting that HO-1 expression by CORM-2 works by an alternate pathway. In conclusion the ability of CO, a product of heme degradation, to induce HO-1 in dermal fibroblasts may serve as a mechanism to amplify HO-1 expression in stressed tissues and may serve as the basis for a novel therapeutic approach for treating chronic wounds.

A thesis submitted to the Faculty of Science, University of the Witwatersrand, Johannesburg, in fulfilment of the requirements for the degree of Doctor of Phllosophy. / A disadvantage of the Fischer-Tropsch synthesis is that a broad product spectrum is obtained. Economic considerations however require an improvement in the optimization of the reaction to maximize the production of high value commercial products, in·particular, short chain olefins and high molecular weight hydrocarbons. [Abbreviated abstract. Open document to view full version] / AC2017

Highly dispersed gold nanoparticles on metal oxide surfaces have recently been reported to exhibit high catalytic activity for low-temperature carbon monoxide oxidation. Amongst the metal oxides, titanium dioxide, more often the commercial form Degussa P25, has been the most studied support for gold as a catalyst for CO oxidation because it yields some of the most active and stable catalysts. Physical and chemical modification of catalysts supports has been shown to affect their catalytic properties. In this research, modified gold supported catalysts have been prepared, characterized and tested for CO oxidation. Their properties have been compared with those of the unmodified catalysts. Catalysts containing1wt% Au supported on MxOy and TiO2/MxOy mixed oxide (M = Zn, Mg, Ni, Fe, Cr, Cu, Mn and Co; TiO2:MxOy mole ratio of 5:1; TiO2 = Degussa P25) were prepared by the single step borohydride reduction method and it was found that TiO2 gave the most superior activity as support for gold for CO oxidation, followed by TiO2/MxOy and the corresponding MxOy. The specific activities for CO oxidation of Au/TiO2 catalysts per unit of prepared in the range 0.05 to 1 wt% of Au indicates that for catalysts prepared by deposition precipitation, there is a significant decrease in specific activities with an increase with gold loading. For the single step borohydride reduction procedure, specific activities decrease less significantly with increasing gold content, implying that for economic and practical reasons, it would be advantageous to prepare gold catalysts with low gold loadings. Cyanide leaching of 1 wt% Au/TiO2 catalysts at different Au:CN- ratios, to selectively remove some of the gold in the catalysts, shows the activity per unit mass of gold to increases as more gold is removed from the catalyst. This is consistent with the idea that gold exists in more than one oxidation state in the systems and a significant fraction of the gold present in the catalysts do not contribute to catalytic activity. A number of anions and cations have been incorporated into TiO2 as support for gold catalysts and also into as-prepared Au/TiO2 catalysts at levels ranging from 0.05 mol% to 2.5 mol% with respect to the support. The activities of the catalysts for CO oxidation reveal that at the highest concentration levels of the ions, in all cases, a decrease in activity compared with unmodified Au/TiO2 is observed. However, addition of 0.05 to 0.4 mol% of the ions with respect to the support, prior to gold addition, in most cases, resulted in activity enhancement which increased with a decrease in the ion content. Similar addition of 0.05 to 0.4 mol% of the ions with respect to TiO2 to Au/TiO2 resulted in a decrease in activity. Attempts to understand the origins of these effects show that there is a degree of chemical interaction between the added ions and gold.

A thesis submitted to the Faculty of Science, University of the Witwatersrand, Johannesburg, in fulfilment of the requirements for the degree of Masters of Science. Johannesburg, 2016 / Gold nanoparticles are ideally suited as catalysts for selected low temperature reactions such as CO oxidation for catalytic convertors in the motor industry due to their high activity. But they are prone to sintering at high temperatures. Platinum-group-metal based catalysts are efficient at elevated temperatures and generally inactive at lower temperatures. This study explored the CO oxidation efficiency of gold nanoparticles and of a combination of gold and rhodium nanoparticles. Variables such as pH, loading concentration and type of support were varied to control the final properties of the Au based catalysts. Possible bimetallic systems of gold and rhodium were explored for wider temperature range activity than gold alone. All catalysts were characterised using Transmission Electron Microscopy (TEM), Energy Dispersive X-ray Spectroscopy (EDS) and X-Ray Diffraction (XRD). Activity was measured using a temperature controlled, custom-built reactor linked to a gas chromatograph. The conditions yielding the smallest gold nanoparticles were established by adding 5, 8 or 10 wt.% loadings of chloroauric acid to aqueous suspensions of either TiO2 or SiO2 at pH 5, 7 or 9 and at 70-75 °C over 60 minutes. Each preparation was sealed in parafilm, aged in the dark at room temperature for 3 days, vacuum-filtered and subsequently calcined at 300 °C. Gold nanoparticles were smallest when deposited onto TiO2 instead of SiO2, at pH 7 and at a loading of 5 wt. %. A combination of gold and rhodium catalysts were subsequently prepared using these conditions, with the simultaneous addition of rhodium at 1, 3, 5 or 10 wt. % loading. Hydrolysis of gold is highly dependent upon pH, resulting in the synthesis of smaller particles under alkaline conditions. Catalytic activity of samples analysed at 70 and 150 °C was highest for gold nanoparticles below 5 nm, in agreement with previous studies. In the proposed bimetallic catalysts, it was difficult to distinguish gold and rhodium nanoparticles in TEM images, although EDS confirmed their combined presence on the TiO2 support. Particle sizes remained below 5 nm, appearing monodispersed on the TiO2 support except at 10 % rhodium loading where some nanoparticle aggregation was observed. CO oxidation activity showed an apparent temperaturedependent shift in the optimal rhodium loading. Au-TiO2 catalysts with a 5% loading showed the highest activity up to 350 °C for a period of 10 hours and the catalyst deactivated due to sintering. At 150 and 200 °C the Au/Rh-TiO2 catalyst remained active for more than 12 hours. It was concluded that the inclusion of rhodium is a potentially-favourable method for stabilising the activity of gold catalysts.

Um dos grandes desafios a ser vencido para a utilização em larga escala das células a combustível de eletrólito polimérico alimentada com H2 obtido por reforma é a contaminação da superfície do eletrocatalisador de Pt, usualmente utilizado no ânodo,pelos gases CO e CO2 presentes no combustível. Neste trabalho é apresentado o estudo dos mecanismos de tolerância de materiais formados por Pt e Mo (Pt/C, Pt3Mo2/C e Pt1Mo1/C) aos contaminadores CO e CO2 e a influência da temperatura nesses processos. Os estudos foram realizados por meio de curvas de polarização com medidas de espectrometria de massas (EM) on line, experimentos de EM em circuito aberto e voltametria linear de remoção de CO adsorvido no catalisador em diferentes temperaturas. Para os catalisadores Pt/C e Pt3 Mo2 /C os resultados mostraram um aumento em 10 vezes na tolerância ao CO quando a temperatura de operação da célula é elevada em 20&deg;C (de 85&deg;C a 105&deg;C) e uma tolerância significativamente superior do Pt3Mo2/C em relação à Pt/C. A ocorrência do mecanismo bifuncional, do mecanismo Eley-Rideal e da reação de Troca Gás-Água (do inglês Water Gas Shift - WGS) foi confirmada apenas para PtMo/C; porém, a diminuição do sobrepotencial de oxidação do CO com o aumento da temperatura foi notada para ambos os catalisadores. A reação de WGS é acelerada com a elevação da temperatura, confirmando que a cinética é a determinante da reação.Também foi realizada a quantificação do cruzamento do O2 do cátodo para o ânodo, sua participação na eliminação do CO e a influência da temperatura nesse processo. Observou-se que a oxidação parcial do CO pelo O2 efetivamente ocorre, aumenta com a temperatura, porém pouco contribui no processo global de tolerância dos catalisadores Pt/C e PtMo/C. Em relação ao contaminante CO3, confirmou-se a ocorrência da reação RWGS (WGS reversa) para ambos os catalisadores, assim como a reação RWGS eletroquímica. Em termos de desempenho de célula,excelentes resultados foram obtidos com a mesma operando a 105&deg;C - para Pt3Mo2/C e utilizando uma mistura de H2/CO(75 ppm)/CO2(25%), observando-se sobrepotencial anódico de apenas 40 mV em relação ao hidrogênio puro em densidade de corrente de 1 Acm-2. / One of the biggest challenges to be overcome for the widespread use of polymer electrolye fuel cellsfueled with H2 obtained by reform is the surface contamination of the Pt electrocatalyst, usually used in the anode, by CO and CO2 present in the fuel stream. This work presents a study of the tolerance mechanisms of CO and CO2 contaminants on electrode materials formed by Pt and Mo (Pt /C, Pt3Mo2 /C, and Pt1Mo1/C) and the influence of temperature on these processes. The studies were performed using polarization curves with on line mass spectrometry measurements (MS), MS experiments at open circuit, and linear sweep CO stripping at different temperatures. For Pt/C and Pt3Mo2/C catalysts, results showed a 10 fold increase in the CO tolerance when the fuel cell operating temperature is raised by 20&deg;C (85&deg;C to 105&deg;C) and a significantly higher tolerance of Pt3Mo2/C compared to Pt/C. The occurrence of the so called bifunctional mechanism, Eley-Rideal mecanism and the Water Gas Shift (WGS) reaction was confirmed only for PtMo/C, but the decrease in the CO oxidation overpotential with the increase of temperature was noted for both catalysts. Also a quantification of O2 crossover from the cathode to the anode was carried out, together with an evaluation of its participation in the elimination of CO and the characterization of influence of temperature in this process. It was observed that the partial oxidation of CO by O2 does occur, increases with temperature, but it has little effect in the overall tolerance of Pt/C and PtMo/Ccatalysts. The WGS reaction is accelerated by increasing the temperature, confirming that the kinetics of the reaction is rate determinant. Regarding CO2 contaminant, the occurrence of the RWGS reaction (reverse WGS) and the electrochemical RWGS were confirmed for both catalysts. In terms of cell performance, excellent results were obtained with the cell operating at 105&deg;C for Pt3Mo2/C and using a mixture of H2/CO (75 ppm)/CO2 (25%), observing an anodic overpotential of only 40 mVcompared to pure hydrogen was observed at a current density of 1 Acm-2.

Yan, Lei. / Thesis (M.Phil.)--Chinese University of Hong Kong, 2007. / Includes bibliographical references (leaves 50-52). / Abstracts in English and Chinese. / Title Page --- p.I / Thesis Committee --- p.II / Abstract --- p.III / 摘要 --- p.IV / Acknowledgements --- p.V / Table of Contents --- p.1 / Chapter Chapter I. --- Introduction --- p.3 / Chapter Chapter II. --- Properties of Hydrogen --- p.6 / Chapter A. --- Spectroscopic Properties of Hydrogen Molecules --- p.6 / Chapter B. --- Properties of Solid Hydrogen --- p.9 / Chapter C. --- Solid Hydrogen as a Matrix Material --- p.12 / Chapter Chapter III. --- Experimental Apparatus --- p.16 / Chapter A. --- Fourier Transformer Spectrometer --- p.16 / Chapter B. --- Cryostat and Sample Cell --- p.23 / Chapter C. --- Gas Handling System and ortho-para Converter --- p.25 / Chapter D. --- Determination of o-H2 Concentration --- p.29 / Chapter E. --- Preparation of Matrix-isolated Species --- p.32 / Chapter Chapter IV. --- Spectroscopic studies of CO in solid hydrogen --- p.34 / Chapter A. --- "Matrix Isolation Spectroscopy of CO, brief overview" --- p.34 / Chapter B. --- Observation and Preliminary Analysis --- p.35 / Chapter i. --- CO in Normal H2 Matrix --- p.35 / Chapter ii. --- CO in Hydrogen Matrix of 50/50 Mixture --- p.37 / Chapter iii. --- CO in Para-enriched Solid Matrix --- p.39 / Chapter C. --- Discussion --- p.46 / Chapter Chapter V. --- Concluding Remarks --- p.48 / Reference --- p.50

Digitized by Kansas Correctional Industries