Abstract
A bench-scale, separate-effect, flow apparatus has been constructed to examine volatile iodine production rates in relation to a selection of the possible variables and conditions found in a containment structure with a breached reactor core. The constructed apparatus is designed to provide the widest possible range of data including gas and aqueous phase speciation for an established set of interfacial mass transfer parameters with known pH and dissolved oxygen levels. As the interfacial transfer of iodine is an important component in the understanding of iodine chemistry, commissioning of the constructed apparatus focused on establishing a well characterized set of mass transfer parameters for a variety of mixing conditions and solution volumes. Aqueous phase parameters, obtained using a method involving the sparging of the dissolved oxygen in the aqueous phase, were found to vary by one order of magnitude, from 1x10{sup -2} to 1x10{sup -3} dm/sec. Gas phase parameters also changeable by one order of magnitude, from 1x10{sup -1} to 1x10{sup -2} dm/sec, were studied more thoroughly as they were found to have a greater impact in the system. Two independent methods of analysis were used, one involving tri-iodide solutions, the other using relative humidity values. A selection of the acquired
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Evans, G J;
Panyan, E J
[1]
- Toronto Univ., ON (Canada). Dept. of Chemical Engineering and Applied Chemistry
Citation Formats
Evans, G J, and Panyan, E J.
Iodine volatilization from irradiated CsI solutions.
Switzerland: N. p.,
1996.
Web.
Evans, G J, & Panyan, E J.
Iodine volatilization from irradiated CsI solutions.
Switzerland.
Evans, G J, and Panyan, E J.
1996.
"Iodine volatilization from irradiated CsI solutions."
Switzerland.
@misc{etde_481713,
title = {Iodine volatilization from irradiated CsI solutions}
author = {Evans, G J, and Panyan, E J}
abstractNote = {A bench-scale, separate-effect, flow apparatus has been constructed to examine volatile iodine production rates in relation to a selection of the possible variables and conditions found in a containment structure with a breached reactor core. The constructed apparatus is designed to provide the widest possible range of data including gas and aqueous phase speciation for an established set of interfacial mass transfer parameters with known pH and dissolved oxygen levels. As the interfacial transfer of iodine is an important component in the understanding of iodine chemistry, commissioning of the constructed apparatus focused on establishing a well characterized set of mass transfer parameters for a variety of mixing conditions and solution volumes. Aqueous phase parameters, obtained using a method involving the sparging of the dissolved oxygen in the aqueous phase, were found to vary by one order of magnitude, from 1x10{sup -2} to 1x10{sup -3} dm/sec. Gas phase parameters also changeable by one order of magnitude, from 1x10{sup -1} to 1x10{sup -2} dm/sec, were studied more thoroughly as they were found to have a greater impact in the system. Two independent methods of analysis were used, one involving tri-iodide solutions, the other using relative humidity values. A selection of the acquired volatility rates in relation to the effect of pH are presented. The apparatus has been found to consistently provide rates up to one order of magnitude lower than modelled predictions. Specifically, for buffered solutions, rates of 2x10{sup -12} mol/min and 1x10{sup -10} mol/min for pH 9 and 5 respectively, have been found. Rates of 1x10{sup -11} mol/min and 6x10{sup -10} mol/min are predicted. Current efforts have addressed potential reasons for this apparent discrepancy, the major factor being the possible release of components from the stainless steel during irradiation. Efforts undertaken to ensure the validity of the results are emphasized. (Abstract Truncated)}
place = {Switzerland}
year = {1996}
month = {Dec}
}
title = {Iodine volatilization from irradiated CsI solutions}
author = {Evans, G J, and Panyan, E J}
abstractNote = {A bench-scale, separate-effect, flow apparatus has been constructed to examine volatile iodine production rates in relation to a selection of the possible variables and conditions found in a containment structure with a breached reactor core. The constructed apparatus is designed to provide the widest possible range of data including gas and aqueous phase speciation for an established set of interfacial mass transfer parameters with known pH and dissolved oxygen levels. As the interfacial transfer of iodine is an important component in the understanding of iodine chemistry, commissioning of the constructed apparatus focused on establishing a well characterized set of mass transfer parameters for a variety of mixing conditions and solution volumes. Aqueous phase parameters, obtained using a method involving the sparging of the dissolved oxygen in the aqueous phase, were found to vary by one order of magnitude, from 1x10{sup -2} to 1x10{sup -3} dm/sec. Gas phase parameters also changeable by one order of magnitude, from 1x10{sup -1} to 1x10{sup -2} dm/sec, were studied more thoroughly as they were found to have a greater impact in the system. Two independent methods of analysis were used, one involving tri-iodide solutions, the other using relative humidity values. A selection of the acquired volatility rates in relation to the effect of pH are presented. The apparatus has been found to consistently provide rates up to one order of magnitude lower than modelled predictions. Specifically, for buffered solutions, rates of 2x10{sup -12} mol/min and 1x10{sup -10} mol/min for pH 9 and 5 respectively, have been found. Rates of 1x10{sup -11} mol/min and 6x10{sup -10} mol/min are predicted. Current efforts have addressed potential reasons for this apparent discrepancy, the major factor being the possible release of components from the stainless steel during irradiation. Efforts undertaken to ensure the validity of the results are emphasized. (Abstract Truncated)}
place = {Switzerland}
year = {1996}
month = {Dec}
}