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Catalytic ozonation of VOCS over different porous materials /Kwong, Chi Wai. January 2009 (has links)
Thesis (Ph.D.)--Hong Kong University of Science and Technology, 2009. / Includes bibliographical references (p. 75-83).
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Generation and detection of ozone and hydroxyl radicals in waterFung, Wai-kit., 馮偉傑. January 2003 (has links)
published_or_final_version / Chemistry / Master / Master of Philosophy
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The electrogeneration of hydroxyl radicals for water disinfection.Mangombo, Zelo January 2006 (has links)
<p>This study has shown that OHË radicals can be generated in an Fe/O2 cell from the electrode products via Fenton&rsquo / s reaction and used for water disinfection. The cell system in which the experiments were carried out was open and undivided and contained two electrodes with iron (Fe) as the anode and oxygen (O2) gas diffusion electrode. Typically, 100 ml of Na2SO4.10H2O (0.5M) solution was used as a background electrolyte. OHË radicals were produced in-situ in an acidic solution aqueous by oxidation of iron (II), formed by dissolving of the anode, with hydrogen peroxide (H2O2). The H2O2 was electrogenerated by reduction of oxygen using porous reticulated vitreous carbon (RVC) as a catalyst.</p>
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Application of ozone as a disinfectant for commercially processed seafoodHansen, Jenny K. 20 May 2002 (has links)
Pacific oysters (Crassostrea gigas), Alaska pink salmon (Oncorynchus
gorbuscha) roe and chum salmon (Oncorynchus keta) fillets were treated with
aqueous ozone in both pilot plant and commercial settings to determine its effect on
shelf-life and microbial changes. The microbial quality was analyzed by conducting
pyschrotrophic and coliform plate counts on 3M petrifilm. Oxidative rancidity, pH
and moisture were measured during the shelf-life study to determine the effects of
ozone on quality. Concentrations of 0.5-1.3 ppm of ozone were applied for periods
of 30 s, 1, 2 and 4 min at 5°C, 9°C and 15°C to determine an optimum ozone
concentration and contact time that would decrease the seafood microbial load and
increase shelf-life in the pilot plant studies. Oysters and roe were treated at 15°C
and 5°C and fillets were treated at 9°C.
There where only minor microbial differences between ozonated and non-ozonated
samples. Treatment temperatures rather than treatment types affected the
microbial load. The pilot plant experiments at 15°C and 5°C showed 1 log
decrease in oysters and roe treated with aqueous ozone at variable concentrations.
No increase in shelf-life was observed when salmon fillets were treated with
aqueous ozone (1.3 ppm) for 2 min. Bacteria strains were isolated from treated (ozone
and water) and control salmon fillet groups at 0, 5 and 10 days of storage and identified
using the API20 NE system. The microbial change in the fillet flora did not differ between
ozonated and non-ozonated treatment groups. Gram-positive bacteria were predominant
in all groups at day 0, Pseudomonas flunrescens and P. putida were the predominant
bacterial species found from all groups at days 5 and 10.
Aqueous ozone (0.5-1.7 ppm) was applied in a commercial Ikura roe processing
facility. A decrease in the microbial load was seen in the pre-processed samples which
were ozonated with eggs in the skein. There were no differences in microbial loads from
the non-ozonated and ozonated post-processed samples of individual eggs removed from
the skein. / Graduation date: 2003
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The electrogeneration of hydroxyl radicals for water disinfection.Mangombo, Zelo January 2006 (has links)
<p>This study has shown that OHË radicals can be generated in an Fe/O2 cell from the electrode products via Fenton&rsquo / s reaction and used for water disinfection. The cell system in which the experiments were carried out was open and undivided and contained two electrodes with iron (Fe) as the anode and oxygen (O2) gas diffusion electrode. Typically, 100 ml of Na2SO4.10H2O (0.5M) solution was used as a background electrolyte. OHË radicals were produced in-situ in an acidic solution aqueous by oxidation of iron (II), formed by dissolving of the anode, with hydrogen peroxide (H2O2). The H2O2 was electrogenerated by reduction of oxygen using porous reticulated vitreous carbon (RVC) as a catalyst.</p>
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Enhancement of the biodegradability of grain distillery wastewater to improve upflow anaerobic sludge blanket reactor efficiency /Gie, Lowna-Marié. January 2007 (has links)
Thesis (MSc)--University of Stellenbosch, 2007. / Bibliography. Also available via the Internet.
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OsoongenereringDenkema, Jacobus Francois 23 June 2014 (has links)
M.Ing. (Electrical & Electronic Engineering) / Please refer to full text to view abstract
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The electrogeneration of hydroxyl radicals for water disinfectionMangombo, Zelo January 2006 (has links)
Magister Scientiae - MSc / This study has shown that OHË radicals can be generated in an Fe/O2 cell from the electrode products via Fenton’s reaction and used for water disinfection. The cell system in which the experiments were carried out was open and undivided and contained two electrodes with iron (Fe) as the anode and oxygen (O2) gas diffusion electrode. Typically, 100 ml of Na2SO4.10H2O (0.5M) solution was used as a background electrolyte. OHË radicals were produced in-situ in an acidic solution aqueous by oxidation of iron (II), formed by dissolving of the anode, with hydrogen peroxide (H2O2). The H2O2 was electrogenerated by reduction of oxygen using porous reticulated vitreous carbon (RVC) as a catalyst. / South Africa
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AN ALTERNATIVE WATER TREATMENT PLAN: MUTAGENIC ACTIVITY OF SELECTED ORGANIC COMPOUNDS TREATED WITH OZONEIrwin, Leslie Annette January 1982 (has links)
No description available.
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An integrated computational fluid dynamics an kinetics study of ozonation in water treatment.Huang, Tzu Hua. January 2005 (has links)
Computational fluid dynamic (CFO) modelling has been applied to examine the operation of the
prc-ozonation system at Wiggins Waterworks, operated by Umgeni Water in Durban, South Africa.
Ozonation is employed in water treatment process primarily to achieve the oxidation of iron and
manganese, the destruction of micro-organisms and the removal of taste and odour causing compounds. It
also aids in the reduction of the colour of the final water, enhancement of algae removal and possible
reduction of coagulant demand.
A hydrodynamic model has been satisfactorily verified by experimental tracer tests. The effect of the gas
injection was modelled by increasing the level of turbulence intensity at the ozone contactor inlet. The
model prediction of the overall tracer response corresponded closely to the experimental results. The
framework of ozone reaction modelling was subsequently established using values of rate constants from
the literature. An accurate prediction of the ozone concentration profile requires the application of the
correct ozone kinetics involved. In raw waters, the depletion of ozone is influenced by the presence of
natural organic matters (NOM). The observed ozone decay was found in good agreement using the pseudo
first-order rate law. By measuring the total organic carbon (TOC) as a surrogate for NOM, the
experimentally determined rate constants can be calculated to account for the effects of the ozone doses and
the water quality. The characterisation study also aimed to provide sufficient information on ozone
depletion and to be operated easily, without the lengthy and costly analyses ofa detailed kinetics study.
The predicted profile of residual ozone concentration suggests the current operating strategy can be
improved to optimise the ozone utilisation. The proposed monitoring point was suggested to be at the end
of second companment where most ozone reactions have been completed. By coupling the transport
equations of the target compounds with their chemical reaction rates, the concentration profile of these
compounds such as ozone can be predicted in order to assist the understanding of an operation and to attain
better interpretation of experimental results. / Thesis (Ph.D.)-University of KwaZulu-Natal, 2005.
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