2010
DOI: 10.1016/j.nucengdes.2010.02.005
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Numerical assessment of pyrochemical process performance for PEACER system

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Cited by 14 publications
(8 citation statements)
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“…Comparatively, this model accounts for more details in the processing, such as flows condition, surface area change, and solubility limits of solutes. There are also other models supported by commercial software, such as ANSYS and COMSOL [115,116,117]. In addition to electrorefining, molten salt clean-up processing is another area needed to be studied since there are still some actinides, rare earth, and active fission products left in removed molten salt.…”
Section: Electrolysis Modelmentioning
confidence: 99%
“…Comparatively, this model accounts for more details in the processing, such as flows condition, surface area change, and solubility limits of solutes. There are also other models supported by commercial software, such as ANSYS and COMSOL [115,116,117]. In addition to electrorefining, molten salt clean-up processing is another area needed to be studied since there are still some actinides, rare earth, and active fission products left in removed molten salt.…”
Section: Electrolysis Modelmentioning
confidence: 99%
“…For electrochemical facilities, a few models of the electrorefiner are being developed that would generate time series of PM residuals [15][16][17][18][19]. The intent is to detect off-normal conditions that could indicate misdirection of Pu.…”
Section: Model-based Predictionsmentioning
confidence: 99%
“…PM data can also include very frequent high-dimensional spectral data from gamma detectors [20][21][22], or low-dimensional flow and/or in-tank volume data from flow meters or in-tank dip tubes. In some cases, PM data can be relatively high quality, such as in-line mass or volume flow measurements, and some current research is aimed at high-quality in-line SNM accountability measurements for electrochemical facilities [14][15][16][17][18][19] and aqueous facilities [7,8,20,21].…”
Section: A11 Nmamentioning
confidence: 99%
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“…In contrast, Bae et al coupled 3D hydrodynamic results with 1D electrochemical kinetic simulation, but the diffusion boundary layer thickness was only calculated with the limited data points of concentration distributions. 21 Recently, several researchers have developed 3D computational models that fully couple electrochemistry and hydrodynamics; however, these models require extensive computational resources and suffer from fully-coupled multispecies calculations. 9,[22][23][24][25][26] Therefore, this paper combines a 3D hydrodynamic model with a 2D multi-species electrochemical model to mitigate the computational costs and address the convergence problem in a fully coupled 3D model.…”
mentioning
confidence: 99%