Thorium oxide dissolution kinetics for hydroxide and carbonate complexation

Thesis (S.M.)--Massachusetts Institute of Technology, Dept. of Nuclear Engineering, 2001. === Includes bibliographical references (p. 64-66). === In order to better understand the behavior of thorium breeder reactor fuel in a repository environment, the behavior of thorium oxide was investigated. Th...

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Main Author: Curran, Virginia, 1977-
Other Authors: Kenneth R. Czerwinski.
Format: Others
Language:English
Published: Massachusetts Institute of Technology 2005
Subjects:
Online Access:http://hdl.handle.net/1721.1/8687
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spelling ndltd-MIT-oai-dspace.mit.edu-1721.1-86872019-05-02T15:44:58Z Thorium oxide dissolution kinetics for hydroxide and carbonate complexation Curran, Virginia, 1977- Kenneth R. Czerwinski. Massachusetts Institute of Technology. Dept. of Nuclear Engineering. Massachusetts Institute of Technology. Dept. of Nuclear Engineering. Nuclear Engineering. Thesis (S.M.)--Massachusetts Institute of Technology, Dept. of Nuclear Engineering, 2001. Includes bibliographical references (p. 64-66). In order to better understand the behavior of thorium breeder reactor fuel in a repository environment, the behavior of thorium oxide was investigated. The kinetics of crystalline thorium oxide dissolution were studied under argon and argon/10% CO2 over a broad pH range in 0.1 M ionic strength NaC1O4 solution. Samples were analyzed for thorium concentration using ICP-AES, ICP-MS, and NAA. Data was fit to a first order kinetics model. The kinetic rate constant under pure argon was 0.0107 ± 0.00123 h-1 for pH 2-3. Under 10% CO2, the rate constant was 0.00511 ± 0.000863 h-1. No kinetics results could be discerned from the data at higher pH. Under argon, solubility at pH greater than 3 was at nm/L levels, three orders of magnitude lower than at pH 3 and below. Under 10% CO2, solubilities decreased from 10 [mu]mol/L at pH 2.06 to 80 nm/Lat pH 3. Thorium oxide powder remnants from each experiment were analysed using XRD, FflR, and BET surface area analysis. Surface area analysis showed a 15% increase in surface area at pH 10 and higher under argon, and a uniform surface area increase of 15 to 30% under 10% CO2. XRD and FfIR spectra showed that the thorium oxide was otherwise identical to the untreated standards. by Virginia Curran. S.M. 2005-08-23T22:21:06Z 2005-08-23T22:21:06Z 2001 2001 Thesis http://hdl.handle.net/1721.1/8687 49747282 eng M.I.T. theses are protected by copyright. They may be viewed from this source for any purpose, but reproduction or distribution in any format is prohibited without written permission. See provided URL for inquiries about permission. http://dspace.mit.edu/handle/1721.1/7582 92 p. 4654264 bytes 4654024 bytes application/pdf application/pdf application/pdf Massachusetts Institute of Technology
collection NDLTD
language English
format Others
sources NDLTD
topic Nuclear Engineering.
spellingShingle Nuclear Engineering.
Curran, Virginia, 1977-
Thorium oxide dissolution kinetics for hydroxide and carbonate complexation
description Thesis (S.M.)--Massachusetts Institute of Technology, Dept. of Nuclear Engineering, 2001. === Includes bibliographical references (p. 64-66). === In order to better understand the behavior of thorium breeder reactor fuel in a repository environment, the behavior of thorium oxide was investigated. The kinetics of crystalline thorium oxide dissolution were studied under argon and argon/10% CO2 over a broad pH range in 0.1 M ionic strength NaC1O4 solution. Samples were analyzed for thorium concentration using ICP-AES, ICP-MS, and NAA. Data was fit to a first order kinetics model. The kinetic rate constant under pure argon was 0.0107 ± 0.00123 h-1 for pH 2-3. Under 10% CO2, the rate constant was 0.00511 ± 0.000863 h-1. No kinetics results could be discerned from the data at higher pH. Under argon, solubility at pH greater than 3 was at nm/L levels, three orders of magnitude lower than at pH 3 and below. Under 10% CO2, solubilities decreased from 10 [mu]mol/L at pH 2.06 to 80 nm/Lat pH 3. Thorium oxide powder remnants from each experiment were analysed using XRD, FflR, and BET surface area analysis. Surface area analysis showed a 15% increase in surface area at pH 10 and higher under argon, and a uniform surface area increase of 15 to 30% under 10% CO2. XRD and FfIR spectra showed that the thorium oxide was otherwise identical to the untreated standards. === by Virginia Curran. === S.M.
author2 Kenneth R. Czerwinski.
author_facet Kenneth R. Czerwinski.
Curran, Virginia, 1977-
author Curran, Virginia, 1977-
author_sort Curran, Virginia, 1977-
title Thorium oxide dissolution kinetics for hydroxide and carbonate complexation
title_short Thorium oxide dissolution kinetics for hydroxide and carbonate complexation
title_full Thorium oxide dissolution kinetics for hydroxide and carbonate complexation
title_fullStr Thorium oxide dissolution kinetics for hydroxide and carbonate complexation
title_full_unstemmed Thorium oxide dissolution kinetics for hydroxide and carbonate complexation
title_sort thorium oxide dissolution kinetics for hydroxide and carbonate complexation
publisher Massachusetts Institute of Technology
publishDate 2005
url http://hdl.handle.net/1721.1/8687
work_keys_str_mv AT curranvirginia1977 thoriumoxidedissolutionkineticsforhydroxideandcarbonatecomplexation
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