Ion exchange kinetics of fission products between molten salt and zeolite-A

被引:19
作者
Shaltry, Michael [1 ,2 ]
Phongikaroon, Supathorn [1 ,2 ]
Simpson, Michael F. [3 ]
机构
[1] Univ Idaho, Ctr Adv Energy Studies, Dept Chem & Mat Engn, Idaho Falls, ID 83401 USA
[2] Univ Idaho, Nucl Engn Program, Idaho Falls, ID 83401 USA
[3] Idaho Natl Lab, Ctr Adv Energy Studies, Idaho Falls, ID 83415 USA
基金
美国能源部;
关键词
Ion exchange; Kinetics; Fission products; Molten salt; Zeolite-A; 2-SITE EQUILIBRIUM-MODEL; ICP-MS DETERMINATION; GEOLOGICAL-MATERIALS; ULTRATRACE ELEMENTS; MULTIVALENT CATIONS; MICROWAVE-OVEN; 4A SYSTEM; DECOMPOSITION; QUANTITATION; CHLORIDES;
D O I
10.1016/j.micromeso.2011.11.035
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Experimentation, data analysis, and modeling of ion exchange kinetics between fission products (cesium and strontium) and zeolite-A beads in molten LiCl-KCl have been performed to support optimization of an electrochemical process to treat used nuclear fuel. Models based on pseudo-first- and pseudo-second-order sorption as well as diffusion have been adapted and compared to experimental data to assess their validity in describing the system. Individual experiments were performed with different concentrations of CsCl or SrCl2 in the LiCl-KCl salt. Zeolite beads were removed from the molten salt at prescribed intervals of time and prepared for analysis by inductively coupled plasma-mass spectrometry. Results indicate maximum cesium (Cs) and strontium (Sr) loading occurred at approximately 31 min and 104 min of contact, respectively. The rate of loading and maximum loading were found to increase with increasing initial concentration of Cs or Sr. Data analysis included determination of rate constants and diffusion coefficients of the proposed models for each experimental condition. Results reveal that the diffusion model provides the best fit to the experimental data with average diffusion coefficients of 2.0 x 10 m(2) s(-1) for Cs and 6.3 x 10(-11) m(2) s(-1) for Sr. This suggests that chemical diffusion is the dominant mechanism of mass transfer. (C) 2011 Elsevier Inc. All rights reserved.
引用
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页码:185 / 189
页数:5
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