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Healthcare-acquired infections (HAIs) cost the National Health Service (NHS) in England in excess of £1 billion per year. One of the main HAIs is caused by the endospore-forming bacterium Clostridium difficile. The most common cause of healthcare-acquired diarrhoea in the developed world, C. difficile was responsible for around 850 deaths in England and Wales in 2011. To help reduce the spread of the HAI-causing bacteria, terminal disinfection of isolation rooms and wards using hydrogen peroxide vapour is actively promoted. The key advantages of hydrogen peroxide vapour are its high oxidation potential which has been reported to inactivate bacteria, fungi and spores. An additional advantage of hydrogen peroxide vapour is that it is relatively environmentally friendly, breaking down into oxygen and water. Investigation into bacterial inactivation kinetics was undertaken at controlled, steady concentrations of hydrogen peroxide vapour in the range of 10 ppm to 90 ppm. An exposure chamber was designed whereby the bacterial spores could be exposed to constant concentrations of hydrogen peroxide for various exposure times. Bacterial spores (1-log10 to 8-log10 cfu) were filter deposited onto membranes to achieve an even layer for consistent exposure of the hydrogen peroxide vapour to the spores. Bacillus subtilis is often used for method development in bacterial studies; advantages are it has been shown to be highly resistant to hydrogen peroxide vapour and is not a human pathogen. Following the method development, different strains of C. difficile (ribotypes 014, 027, 103 and 220) were exposed to identify differences in resistance. Inactivation models (Chick-Watson, Series-Event, Weibull and Baranyi) were used to fit the data generated using the environmental chamber. Decimal reduction values (D-values) were calculated from the models for comparative studies regarding the inactivation achieved for the different bacteria and different hydrogen peroxide concentrations. The findings from this thesis revealed the Weibull model provides the best fit for most of the data. An initial shoulder period was identified for B. subtilis which was absent for C. difficile inactivation by hydrogen peroxide vapour; B. subtilis is therefore more resistant to hydrogen peroxide disinfection than C. difficile. Typical D-values for B. subtilis and C. difficile when exposed to hydrogen peroxide vapour at a concentration of 90 ppm were 140 and 1 min, respectively. C. difficile inactivation data were used to develop a model to estimate the log reduction that could be achieved during an inactivation cycle based on the concentration-time integral ( ). This model could be used to estimate the log reduction of commercially available hydrogen peroxide decontamination systems; these release a fixed amount of hydrogen peroxide into the room resulting in a peak concentration before decomposition to oxygen and water. Releasing the hydrogen peroxide into the room in this manner results in spatial and temporal variation; this could result in differences in bacterial inactivation in different areas within the room. Using the aforementioned regression model, the inactivation achieved at all locations within the room could be predicted, which could be used to optimise the current hydrogen peroxide decontamination cycles.

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The next generation of miniaturized satellites (“nanosats”) feature dramatically reduced thrust and impulse requirements for purposes of spacecraft attitude control and maneuvering. E↵orts at the University of Vermont have concentrated on developing a MEMS-based chemical micropropulsion system based on a rocket grade hydrogen peroxide (HTP) monopropellant fuel. A key component in the micropropulsion system is the catalytic reactor whose role is to chemically decompose the monopropellant, thereby releasing the fuel’s chemical energy for thrust production. The present study is a joint computational and experimental design e↵ort at developing a MEMS-based micro-reactor for incorporation into a monopropellant micropropulsion system. Numerically, 0D and simplified 2D models have been developed to validate the model and characterize heat and mass di↵usion in the channel. This model will then be extended to a 2D model including all geometric complexities of the catalyst bed geometry with the goal of optimization. Experimentally, both meso and micro scale catalyst geometries have been constructed to prove the feasibility of using RuO2 nanostructures as an in situ in a microchannel.

Thesis (M.A.)--Boston University / PLEASE NOTE: Boston University Libraries did not receive an Authorization To Manage form for this thesis or dissertation. It is therefore not openly accessible, though it may be available by request. If you are the author or principal advisor of this work and would like to request open access for it, please contact us at open-help@bu.edu. Thank you. / In work reported by Lichtin, Rosenberg, and Imamuras it was found that water added before irradiation of aerated methanol had a surprising effect on peroxide yields. In the absence of water, no hydrogen peroxide was produced during radiolysis, but in the presence of about 0.5 weight-percent water the yield of peroxide increased abruptly from zero to a plateau G value of 2.8. Attempts to reproduce these data were unsuccessful, however, and it was discovered that the observed effect of water on hydrogen peroxide yields is post-radiolytic in nature. Identical peroxide yields were produced during radiolysis of both dry methanol samples and samples to which water was added before radiolysis. In the dry samples, however, hydrogen peroxide was found to decompose with approximately first-order kinetics. Addition of water subsequent to irradiation inhibited decay. No significant change was noted in the concentration of radiolytically-generated formaldehyde during the period of peroxide decay. The average G(H2o2), obtained by extrapolation of the decomposition curve of radiolytically-generated hydrogen peroxide in dry methanol back to the time of the removal ofthe sample from the 60Co source, was 3.28 + 0.12. Half-decay times varied widely due to the variable dryness of the methanol. It was found that solutions of non-radiolytic hydrogen peroxide in dry methanol likewise underwent first-order decay. The rate of decomposition in these solutions could be accelerated by an increase in temperature or by subsequent radiolysis. The addition of formaldehyde was also found to accelerate peroxide decomposition, although no significant change was noted in the formaldehyde concentration. Methyl hydroperoxide was tentatively identified as a radiation product with a G value of about 0.2. Analysis of a radiolytic sample in which hydrogen peroxide had decomposed completely indicated that methyl hydroperoxide had not undergone similar decay. The nature of the hydrogen peroxide decomposition process is still unknown. Speculation concerning the decay inhibiting effect of water has been developed from several points of view: medium effects, specific interactions, and the possible effects of impurity. Influences of added sulfuric acid and methyl borate on radiolytic peroxide yields were also studied briefly. / 2031-01-01

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No description available.

Thesis (M. Sc.) -- Lincoln University, 2006.

Made available in DSpace on 2014-10-09T12:54:53Z (GMT). No. of bitstreams: 0 / Made available in DSpace on 2014-10-09T14:07:04Z (GMT). No. of bitstreams: 1 12797.pdf: 513559 bytes, checksum: 4b6e71bdbea803b32a3222d0b42f7b13 (MD5) / Dissertacao (Mestrado Profissionalizante em Lasers em Odontologia) / IPEN/D-MPLO / Instituto de Pesquisas Energeticas e Nucleares - IPEN/CNEN-SP; Faculdade de Odontologia, Universidade de Sao Paulo, Sao Paulo