Lithium-Ion Model Reactions

The lithium ion battery model inherently assumes an electroneutral, binary mixture of reaction components.

Butler-Volmer Relationship

With only a single scalar modelled for all chemical components, a single reaction is modelled for the lithium intercalation:
Figure 1. EQUATION_DISPLAY
Li + + e + Site Li
(4157)

This reaction rate expression still accounts for concentration variations of different reaction components, and as such is different from the formulations in the previous section (Electrochemical Surface Reactions (Heterogeneous)).

The Butler-Volmer relationship is used to compute the solid electrolyte interface (SEI) normal component of the electric current density j n , s = - j n , l , written as:

Figure 2. EQUATION_DISPLAY
j n , s = j 0 ( e α a F η R u T - e - α c F η R u T ) + C t ( ϕ s - ϕ l )
(4158)
Figure 3. EQUATION_DISPLAY
j 0 = F K ( c s c s , max ) α 1 ( 1 c s c s , max ) α 2 ( c l c l , ref ) α 3
(4159)
where:
  • C is the double-layer capacitance
  • c l is the lithium ion/salt concentration
  • c s is the combined concentration of intercalated lithium in the solid
  • c s , max is the maximum combined concentration of intercalated lithium in the solid
  • c l , ref is a molar reference concentration of lithium cations in the electrolyte

The first term in Eqn. (4159) represents the solid lithium concentration in the reaction, the last term represents the lithium ions in the electrolyte, and the intermediate term represents vacancies in the intercalation material.

The SEI surface overpotential η is computed as

Figure 4. EQUATION_DISPLAY
η = ϕ s - ϕ l - U eq - j n , s R SEI
(4160)

The rate coefficient K depends on temperature according to:

Figure 5. EQUATION_DISPLAY
K = K 0 e - E a R u T
(4161)

Similarly, the electrical resistance of the SEI is dependent on temperature:

Figure 6. EQUATION_DISPLAY
R SEI = R 0 e E SEI R u T
(4162)
where E S E I is the SEI activation energy.