Journal of Applied Electrochemistry

, Volume 48, Issue 6, pp 725–737 | Cite as

Effect of the design parameters on mass transfer and energy consumption inside a lithium electrolysis cell

  • Elaheh Oliaii
  • Martin Désilets
  • Gaétan Lantagne
Research Article

Abstract

A 2D axisymmetric electrochemical model of a lithium experimental cell is solved using a finite element method. The model is considering the coupled effect of momentum, electric, kinetic and mass transfer phenomena. The dense diaphragm used in the setup, which is not hydraulically permeable, separates the cell into two regions: 1 (a) turbulent region, between the anode and the diaphragm, and 2 (a) laminar region between the diaphragm and the cathode. The k-epsilon model is used to solve the turbulent flow resulting from bubbles generation at the anode. A two-phase flow model is also developed to simulate the volume fractions of bubbles and electrolyte in the cell. The non-uniform bubbles distribution over the anode surface, derived from the non-uniform current distribution, has been added to the two-phase model. The effects of the diaphragm length, position and porosity on the electric and two-phase flow fields are simulated. In fact, the diaphragm position and length both influence the current distribution at the surface of electrodes and the velocity distribution in the cell, all of which influence ohmic and kinetic overpotentials. The results show that up to 40% of energy can be saved when running the lithium electrolysis cell with a shorter porous diaphragm located as far as possible from the anode. The maximum current density, found at the bottom corner of anode, is higher when the diaphragm is longer and when it is closer to the anode.

Graphical Abstract

Keywords

Lithium electrochemical cell Mass transfer Turbulent two-phase flow Finite element model 

List of symbols

A

Area (m2)

CD

Drag coefficient

c

Concentration (mol m−3)

Deff

Effective diffusion coefficient (m2 s−1)

db

Bubble diameter (m)

F

Faraday’s constant (A s mol−1)

Fb

Volume force (kg m s−2)

FD

Drag force (kg m s−2)

g

Gravity acceleration constant (m s−2)

i

Local current density (A m−2)

i0

Exchange current density (A m−2)

k

Turbulent kinetic energy (m2 s−2)

L

Length (m)

M

Molecular weight (kg mol−1)

N

Ions flux (mol m−2 s−1)

N

Normal vector

p

Pressure (kg m−1 s−2)

R

Gas constant (J K−1 mol−1)

Re

Reynolds number

T

Temperature (K)

\({\text{T}}_{{\text{k}}}^{{{\text{turb}}}}\)

Stress tensor (kg m−1 s−2)

t

Time (s)

u

Velocity magnitude (m s−1)

um

Mobility (m2 s−1 V−1)

ut

Bubbles terminal velocity (m s−1)

V

Velocity vector (m s−1)

x

Mole fraction

z

Charge number

Greek letters

α0

Transfer coefficient

σ

Electrolyte conductivity (S m−1)

\(\epsilon\)

Rate of dissipation of kinetic energy (m2 s−3)

ε

Porosity

\({{{\upeta}}}\)

Activation overpotential (V)

µ

Viscosity (kg m−1 s−1)

\({{{\uprho}}}\)

Density (kg m−3)

τ

Tortuosity

φ

Volume fraction

\({\emptyset _{\text{g}}}\)

Bubble coverage

Subscripts and superscripts

a

Anode

c

Continuous phase

d

Disperse phase

dia

Diaphragm

i

Species i

in

Inlet

h

Hyperpolarization

mean

Mean

mix

Resistive layer

T

Turbulent

Notes

Acknowledgements

The authors wish to thank Dr. Kamyab Amouzegar for his useful suggestions. We also appreciate Hydro-Québec for their financial support, for providing us with the experimental results and giving us the opportunity to publish this work. The authors are also grateful to the Natural Sciences and Engineering Council of Canada (NSERC) for its financial support.

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Copyright information

© Springer Science+Business Media B.V., part of Springer Nature 2018

Authors and Affiliations

  1. 1.Department of Chemical and Biotechnological EngineeringUniversité de SherbrookeSherbrookeCanada
  2. 2.IREQ (Hydro-Québec’s Research Institute)VarennesCanada

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