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The role of correlations in the determination of the transport properties of LaCl3 in high temperature molten eutectic LiCl–KCl

  • Adib Samin EMAIL logo , Evan Wu and Jinsuo Zhang
Published/Copyright: March 13, 2017

Abstract

It is important to develop an accurate assessment of fundamental data of lanthanides in high temperature molten salts to enable an efficient application of pyroprocessing. This requires a careful consideration of uncertainties in the reported results. In this study, cyclic voltammetry (CV) tests of LaCl3 in KCl–LiCl molten salt were conducted at low concentration levels in the molten salt at 723 K and at several scan rates. The CV signals were subsequently analyzed through the conventional CV analysis and using a BET-based model through a nonlinear least-squares fitting procedure. It was determined that the parameters of the model were strongly correlated and the support plane procedure was implemented to assign joint confidence intervals for the diffusivity of lanthanum. Accounting for the correlations led to a significant increase in the uncertainty of the reported diffusivity which led to better agreement with the literature. Accounting for the correlations may be important for higher concentration levels.

Acknowlegements

The authors would like to acknowledge the U.S. Department of Energy DOE-NEUP program, project number 14-6489 for supporting this research.

Appendix A

The diffusion equation governs both species’ concentrations in the solution:

(11)cOt=DO2cOx2
(12)cRt=DR2cRx2

In these equations, cO and cR are the concentrations of the oxidized and reduced species, respectively. The domain on which the equations are solved is 0≤xL, where we choose L=12DTmax (Tmax is the time needed for one full CV cycle). The product is assumed to have a very low diffusivity [DR~O(10−20) cm2/s]. In addition, the adsorption on the electrode is described by the BET isotherm [20]:

(13)ΓR(t)=ΓsK1cR(0,t)(1KdcR(0,t))(1+K1cR(0,t)KdcR(0,t))

Here, Γs is the maximum surface concentration of the product species, and K1 and Kd are the adsorption and desorption equilibrium constants. Finally, the boundary conditions for the diffusion equations at the electrode surface describe the kinetics of the reaction. The boundary conditions sufficiently far from the electrode surface are assumed equal to the bulk concentration values:

(14)DOcOx|x=0=cO(0,t)kf0eαnFRT(EEf0)cR(0,t)kb0e(1α)nFRT(EEf0)
(15)DRcRx|x=0=dΓRdtcO(0,t)kf0eαnFRT(EEf0)+cR(0,t)kb0e(1α)nFRT(EEf0)

In the equations, Ef0 is the formal potential, kf0 and kb0 are the reaction rates for the forward and backward directions, respectively evaluated at the formal potential, F is Farad’s constant, R is the universal gas constant, T is the temperature and α is the charge transfer coefficient. In all our simulations we assumed kf0=kb0=k0. The initial conditions and the boundary conditions away from the electrode were selected as follows:

(16)cO(x,t=0)=cO(L,t)=cbulk;cR(x,t=0)=cR(L,t)=0;ΓP(t=0)=0

In the model, the current was defined as:

(17)I=nFADOcOx|x=0

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Received: 2016-10-18
Accepted: 2017-1-27
Published Online: 2017-3-13
Published in Print: 2017-7-26

©2017 Walter de Gruyter GmbH, Berlin/Boston

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