def set_events(self, variables):
eps_n = variables["Negative electrode porosity"]
eps_p = variables["Positive electrode porosity"]
self.events.append(
pybamm.Event(
"Zero negative electrode porosity cut-off",
pybamm.min(eps_n),
pybamm.EventType.TERMINATION,
))
self.events.append(
pybamm.Event(
"Max negative electrode porosity cut-off",
pybamm.max(eps_n) - 1,
pybamm.EventType.TERMINATION,
))
self.events.append(
pybamm.Event(
"Zero positive electrode porosity cut-off",
pybamm.min(eps_p),
pybamm.EventType.TERMINATION,
))
self.events.append(
pybamm.Event(
"Max positive electrode porosity cut-off",
pybamm.max(eps_p) - 1,
pybamm.EventType.TERMINATION,
))
def test_special_functions(self):
a = pybamm.Array(np.array([1, 2, 3, 4, 5]))
self.assert_casadi_equal(pybamm.max(a).to_casadi(),
casadi.MX(5),
evalf=True)
self.assert_casadi_equal(pybamm.min(a).to_casadi(),
casadi.MX(1),
evalf=True)
b = pybamm.Array(np.array([-2]))
c = pybamm.Array(np.array([3]))
self.assert_casadi_equal(pybamm.Function(np.abs, b).to_casadi(),
casadi.MX(2),
evalf=True)
self.assert_casadi_equal(pybamm.Function(np.abs, c).to_casadi(),
casadi.MX(3),
evalf=True)
for np_fun in [
np.sqrt,
np.tanh,
np.cosh,
np.sinh,
np.exp,
np.log,
np.sign,
np.sin,
np.cos,
np.arccosh,
np.arcsinh,
]:
self.assert_casadi_equal(pybamm.Function(np_fun, c).to_casadi(),
casadi.MX(np_fun(3)),
evalf=True)
def test_special_functions(self):
a = pybamm.Array(np.array([1, 2, 3, 4, 5]))
self.assertEqual(pybamm.max(a).to_casadi(), casadi.SX(5))
self.assertEqual(pybamm.min(a).to_casadi(), casadi.SX(1))
b = pybamm.Array(np.array([-2]))
c = pybamm.Array(np.array([3]))
self.assertEqual(pybamm.Function(np.abs, b).to_casadi(), casadi.SX(2))
self.assertEqual(pybamm.Function(np.abs, c).to_casadi(), casadi.SX(3))
def set_events(self, variables):
c_s_surf = variables[self.domain + " particle surface concentration"]
tol = 0.01
self.events["Minumum " + self.domain.lower() +
" particle surface concentration"] = (
pybamm.min(c_s_surf) - tol)
self.events["Maximum " + self.domain.lower() +
" particle surface concentration"] = (
1 - tol) - pybamm.max(c_s_surf)
def test_special_functions(self):
a = pybamm.Array(np.array([1, 2, 3, 4, 5]))
self.assert_casadi_equal(pybamm.max(a).to_casadi(),
casadi.MX(5),
evalf=True)
self.assert_casadi_equal(pybamm.min(a).to_casadi(),
casadi.MX(1),
evalf=True)
b = pybamm.Array(np.array([-2]))
c = pybamm.Array(np.array([3]))
self.assert_casadi_equal(pybamm.Function(np.abs, b).to_casadi(),
casadi.MX(2),
evalf=True)
self.assert_casadi_equal(pybamm.Function(np.abs, c).to_casadi(),
casadi.MX(3),
evalf=True)
def set_events(self, variables):
c_s_surf = variables[self.domain + " particle surface concentration"]
tol = 0.01
self.events.append(
pybamm.Event(
"Minumum " + self.domain.lower() +
" particle surface concentration",
pybamm.min(c_s_surf) - tol,
pybamm.EventType.TERMINATION,
))
self.events.append(
pybamm.Event(
"Maximum " + self.domain.lower() +
" particle surface concentration",
(1 - tol) - pybamm.max(c_s_surf),
pybamm.EventType.TERMINATION,
))
def __init__(self, name="Doyle-Fuller-Newman half cell model", options=None):
super().__init__({}, name)
pybamm.citations.register("marquis2019asymptotic")
# `param` is a class containing all the relevant parameters and functions for
# this model. These are purely symbolic at this stage, and will be set by the
# `ParameterValues` class when the model is processed.
param = self.param
options = options or {"working electrode": None}
if options["working electrode"] not in ["negative", "positive"]:
raise ValueError(
"The option 'working electrode' should be either 'positive'"
" or 'negative'"
)
self.options.update(options)
working_electrode = options["working electrode"]
######################
# Variables
######################
# Variables that depend on time only are created without a domain
Q = pybamm.Variable("Discharge capacity [A.h]")
# Define some useful scalings
pot = param.potential_scale
i_typ = param.current_scale
# Variables that vary spatially are created with a domain. Depending on
# which is the working electrode we need to define a set variables or another
if working_electrode == "negative":
# Electrolyte concentration
c_e_n = pybamm.Variable(
"Negative electrolyte concentration", domain="negative electrode"
)
c_e_s = pybamm.Variable(
"Separator electrolyte concentration", domain="separator"
)
# Concatenations combine several variables into a single variable, to
# simplify implementing equations that hold over several domains
c_e = pybamm.Concatenation(c_e_n, c_e_s)
# Electrolyte potential
phi_e_n = pybamm.Variable(
"Negative electrolyte potential", domain="negative electrode"
)
phi_e_s = pybamm.Variable(
"Separator electrolyte potential", domain="separator"
)
phi_e = pybamm.Concatenation(phi_e_n, phi_e_s)
# Particle concentrations are variables on the particle domain, but also
# vary in the x-direction (electrode domain) and so must be provided with
# auxiliary domains
c_s_n = pybamm.Variable(
"Negative particle concentration",
domain="negative particle",
auxiliary_domains={"secondary": "negative electrode"},
)
# Set concentration in positive particle to be equal to the initial
# concentration as it is not the working electrode
x_p = pybamm.PrimaryBroadcast(
pybamm.standard_spatial_vars.x_p, "positive particle"
)
c_s_p = param.c_n_init(x_p)
# Electrode potential
phi_s_n = pybamm.Variable(
"Negative electrode potential", domain="negative electrode"
)
# Set potential in positive electrode to be equal to the initial OCV
phi_s_p = param.U_p(pybamm.surf(param.c_p_init(x_p)), param.T_init)
else:
c_e_p = pybamm.Variable(
"Positive electrolyte concentration", domain="positive electrode"
)
c_e_s = pybamm.Variable(
"Separator electrolyte concentration", domain="separator"
)
# Concatenations combine several variables into a single variable, to
# simplify implementing equations that hold over several domains
c_e = pybamm.Concatenation(c_e_s, c_e_p)
# Electrolyte potential
phi_e_s = pybamm.Variable(
"Separator electrolyte potential", domain="separator"
)
phi_e_p = pybamm.Variable(
"Positive electrolyte potential", domain="positive electrode"
)
phi_e = pybamm.Concatenation(phi_e_s, phi_e_p)
# Particle concentrations are variables on the particle domain, but also
# vary in the x-direction (electrode domain) and so must be provided with
# auxiliary domains
c_s_p = pybamm.Variable(
"Positive particle concentration",
domain="positive particle",
auxiliary_domains={"secondary": "positive electrode"},
)
# Set concentration in negative particle to be equal to the initial
# concentration as it is not the working electrode
x_n = pybamm.PrimaryBroadcast(
pybamm.standard_spatial_vars.x_n, "negative particle"
)
c_s_n = param.c_n_init(x_n)
# Electrode potential
phi_s_p = pybamm.Variable(
"Positive electrode potential", domain="positive electrode"
)
# Set potential in negative electrode to be equal to the initial OCV
phi_s_n = param.U_n(pybamm.surf(param.c_n_init(x_n)), param.T_init)
# Constant temperature
T = param.T_init
######################
# Other set-up
######################
# Current density
i_cell = param.current_with_time
# Porosity and Tortuosity
# Primary broadcasts are used to broadcast scalar quantities across a domain
# into a vector of the right shape, for multiplying with other vectors
eps_n = pybamm.PrimaryBroadcast(
pybamm.Parameter("Negative electrode porosity"), "negative electrode"
)
eps_s = pybamm.PrimaryBroadcast(
pybamm.Parameter("Separator porosity"), "separator"
)
eps_p = pybamm.PrimaryBroadcast(
pybamm.Parameter("Positive electrode porosity"), "positive electrode"
)
if working_electrode == "negative":
eps = pybamm.Concatenation(eps_n, eps_s)
tor = pybamm.Concatenation(eps_n ** param.b_e_n, eps_s ** param.b_e_s)
else:
eps = pybamm.Concatenation(eps_s, eps_p)
tor = pybamm.Concatenation(eps_s ** param.b_e_s, eps_p ** param.b_e_p)
# Interfacial reactions
# Surf takes the surface value of a variable, i.e. its boundary value on the
# right side. This is also accessible via `boundary_value(x, "right")`, with
# "left" providing the boundary value of the left side
c_s_surf_n = pybamm.surf(c_s_n)
c_s_surf_p = pybamm.surf(c_s_p)
if working_electrode == "negative":
j0_n = param.j0_n(c_e_n, c_s_surf_n, T) / param.C_r_n
j_n = (
2
* j0_n
* pybamm.sinh(
param.ne_n / 2 * (phi_s_n - phi_e_n - param.U_n(c_s_surf_n, T))
)
)
j_s = pybamm.PrimaryBroadcast(0, "separator")
j_p = pybamm.PrimaryBroadcast(0, "positive electrode")
j = pybamm.Concatenation(j_n, j_s)
else:
j0_p = param.gamma_p * param.j0_p(c_e_p, c_s_surf_p, T) / param.C_r_p
j_p = (
2
* j0_p
* pybamm.sinh(
param.ne_p / 2 * (phi_s_p - phi_e_p - param.U_p(c_s_surf_p, T))
)
)
j_s = pybamm.PrimaryBroadcast(0, "separator")
j_n = pybamm.PrimaryBroadcast(0, "negative electrode")
j = pybamm.Concatenation(j_s, j_p)
######################
# State of Charge
######################
I = param.dimensional_current_with_time
# The `rhs` dictionary contains differential equations, with the key being the
# variable in the d/dt
self.rhs[Q] = I * param.timescale / 3600
# Initial conditions must be provided for the ODEs
self.initial_conditions[Q] = pybamm.Scalar(0)
######################
# Particles
######################
if working_electrode == "negative":
# The div and grad operators will be converted to the appropriate matrix
# multiplication at the discretisation stage
N_s_n = -param.D_n(c_s_n, T) * pybamm.grad(c_s_n)
self.rhs[c_s_n] = -(1 / param.C_n) * pybamm.div(N_s_n)
# Boundary conditions must be provided for equations with spatial
# derivatives
self.boundary_conditions[c_s_n] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
-param.C_n * j_n / param.a_R_n / param.D_n(c_s_surf_n, T),
"Neumann",
),
}
# c_n_init can in general be a function of x
# Note the broadcasting, for domains
x_n = pybamm.PrimaryBroadcast(
pybamm.standard_spatial_vars.x_n, "negative particle"
)
self.initial_conditions[c_s_n] = param.c_n_init(x_n)
# Events specify points at which a solution should terminate
self.events += [
pybamm.Event(
"Minimum negative particle surface concentration",
pybamm.min(c_s_surf_n) - 0.01,
),
pybamm.Event(
"Maximum negative particle surface concentration",
(1 - 0.01) - pybamm.max(c_s_surf_n),
),
]
else:
# The div and grad operators will be converted to the appropriate matrix
# multiplication at the discretisation stage
N_s_p = -param.D_p(c_s_p, T) * pybamm.grad(c_s_p)
self.rhs[c_s_p] = -(1 / param.C_p) * pybamm.div(N_s_p)
# Boundary conditions must be provided for equations with spatial
# derivatives
self.boundary_conditions[c_s_p] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
-param.C_p
* j_p
/ param.a_R_p
/ param.gamma_p
/ param.D_p(c_s_surf_p, T),
"Neumann",
),
}
# c_p_init can in general be a function of x
# Note the broadcasting, for domains
x_p = pybamm.PrimaryBroadcast(
pybamm.standard_spatial_vars.x_p, "positive particle"
)
self.initial_conditions[c_s_p] = param.c_p_init(x_p)
# Events specify points at which a solution should terminate
self.events += [
pybamm.Event(
"Minimum positive particle surface concentration",
pybamm.min(c_s_surf_p) - 0.01,
),
pybamm.Event(
"Maximum positive particle surface concentration",
(1 - 0.01) - pybamm.max(c_s_surf_p),
),
]
######################
# Current in the solid
######################
eps_s_n = pybamm.Parameter("Negative electrode active material volume fraction")
eps_s_p = pybamm.Parameter("Positive electrode active material volume fraction")
if working_electrode == "negative":
sigma_eff_n = param.sigma_n * eps_s_n ** param.b_s_n
i_s_n = -sigma_eff_n * pybamm.grad(phi_s_n)
self.boundary_conditions[phi_s_n] = {
"left": (
i_cell / pybamm.boundary_value(-sigma_eff_n, "left"),
"Neumann",
),
"right": (pybamm.Scalar(0), "Neumann"),
}
# The `algebraic` dictionary contains differential equations, with the key
# being the main scalar variable of interest in the equation
self.algebraic[phi_s_n] = pybamm.div(i_s_n) + j_n
# Initial conditions must also be provided for algebraic equations, as an
# initial guess for a root-finding algorithm which calculates consistent
# initial conditions
self.initial_conditions[phi_s_n] = param.U_n(
param.c_n_init(0), param.T_init
)
else:
sigma_eff_p = param.sigma_p * eps_s_p ** param.b_s_p
i_s_p = -sigma_eff_p * pybamm.grad(phi_s_p)
self.boundary_conditions[phi_s_p] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
i_cell / pybamm.boundary_value(-sigma_eff_p, "right"),
"Neumann",
),
}
self.algebraic[phi_s_p] = pybamm.div(i_s_p) + j_p
# Initial conditions must also be provided for algebraic equations, as an
# initial guess for a root-finding algorithm which calculates consistent
# initial conditions
self.initial_conditions[phi_s_p] = param.U_p(
param.c_p_init(1), param.T_init
)
######################
# Electrolyte concentration
######################
N_e = -tor * param.D_e(c_e, T) * pybamm.grad(c_e)
self.rhs[c_e] = (1 / eps) * (
-pybamm.div(N_e) / param.C_e + (1 - param.t_plus(c_e)) * j / param.gamma_e
)
dce_dx = (
-(1 - param.t_plus(c_e))
* i_cell
* param.C_e
/ (tor * param.gamma_e * param.D_e(c_e, T))
)
if working_electrode == "negative":
self.boundary_conditions[c_e] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (pybamm.boundary_value(dce_dx, "right"), "Neumann"),
}
else:
self.boundary_conditions[c_e] = {
"left": (pybamm.boundary_value(dce_dx, "left"), "Neumann"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[c_e] = param.c_e_init
self.events.append(
pybamm.Event(
"Zero electrolyte concentration cut-off", pybamm.min(c_e) - 0.002
)
)
######################
# Current in the electrolyte
######################
i_e = (param.kappa_e(c_e, T) * tor * param.gamma_e / param.C_e) * (
param.chi(c_e, T) * pybamm.grad(c_e) / c_e - pybamm.grad(phi_e)
)
self.algebraic[phi_e] = pybamm.div(i_e) - j
ref_potential = param.U_n_ref / pot
if working_electrode == "negative":
self.boundary_conditions[phi_e] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (ref_potential, "Dirichlet"),
}
else:
self.boundary_conditions[phi_e] = {
"left": (ref_potential, "Dirichlet"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[phi_e] = ref_potential
######################
# (Some) variables
######################
L_Li = pybamm.Parameter("Lithium counter electrode thickness [m]")
sigma_Li = pybamm.Parameter("Lithium counter electrode conductivity [S.m-1]")
j_Li = pybamm.Parameter(
"Lithium counter electrode exchange-current density [A.m-2]"
)
if working_electrode == "negative":
voltage = pybamm.boundary_value(phi_s_n, "left") - ref_potential
voltage_dim = pot * pybamm.boundary_value(phi_s_n, "left")
vdrop_Li = 2 * pybamm.arcsinh(
i_cell * i_typ / j_Li
) + L_Li * i_typ * i_cell / (sigma_Li * pot)
vdrop_Li_dim = (
2 * pot * pybamm.arcsinh(i_cell * i_typ / j_Li)
+ L_Li * i_typ * i_cell / sigma_Li
)
else:
voltage = pybamm.boundary_value(phi_s_p, "right") - ref_potential
voltage_dim = param.U_p_ref + pot * voltage
vdrop_Li = -(
2 * pybamm.arcsinh(i_cell * i_typ / j_Li)
+ L_Li * i_typ * i_cell / (sigma_Li * pot)
)
vdrop_Li_dim = -(
2 * pot * pybamm.arcsinh(i_cell * i_typ / j_Li)
+ L_Li * i_typ * i_cell / sigma_Li
)
c_s_surf_p_av = pybamm.x_average(c_s_surf_p)
c_s_surf_n_av = pybamm.x_average(c_s_surf_n)
# The `variables` dictionary contains all variables that might be useful for
# visualising the solution of the model
self.variables = {
"Time [s]": param.timescale * pybamm.t,
"Negative particle surface concentration": c_s_surf_n,
"X-averaged negative particle surface concentration": c_s_surf_n_av,
"Negative particle concentration": c_s_n,
"Negative particle surface concentration [mol.m-3]": param.c_n_max
* c_s_surf_n,
"X-averaged negative particle surface concentration "
"[mol.m-3]": param.c_n_max * c_s_surf_n_av,
"Negative particle concentration [mol.m-3]": param.c_n_max * c_s_n,
"Electrolyte concentration": c_e,
"Electrolyte concentration [mol.m-3]": param.c_e_typ * c_e,
"Positive particle surface concentration": c_s_surf_p,
"X-averaged positive particle surface concentration": c_s_surf_p_av,
"Positive particle concentration": c_s_p,
"Positive particle surface concentration [mol.m-3]": param.c_p_max
* c_s_surf_p,
"X-averaged positive particle surface concentration "
"[mol.m-3]": param.c_p_max * c_s_surf_p_av,
"Positive particle concentration [mol.m-3]": param.c_p_max * c_s_p,
"Current [A]": I,
"Negative electrode potential": phi_s_n,
"Negative electrode potential [V]": pot * phi_s_n,
"Negative electrode open circuit potential": param.U_n(c_s_surf_n, T),
"Electrolyte potential": phi_e,
"Electrolyte potential [V]": -param.U_n_ref + pot * phi_e,
"Positive electrode potential": phi_s_p,
"Positive electrode potential [V]": (param.U_p_ref - param.U_n_ref)
+ pot * phi_s_p,
"Positive electrode open circuit potential": param.U_p(c_s_surf_p, T),
"Voltage drop": voltage,
"Voltage drop [V]": voltage_dim,
"Terminal voltage": voltage + vdrop_Li,
"Terminal voltage [V]": voltage_dim + vdrop_Li_dim,
}
def __init__(self, name="Doyle-Fuller-Newman model"):
super().__init__({}, name)
# `param` is a class containing all the relevant parameters and functions for
# this model. These are purely symbolic at this stage, and will be set by the
# `ParameterValues` class when the model is processed.
param = self.param
######################
# Variables
######################
# Variables that depend on time only are created without a domain
Q = pybamm.Variable("Discharge capacity [A.h]")
# Variables that vary spatially are created with a domain
c_e_n = pybamm.Variable(
"Negative electrolyte concentration",
domain="negative electrode",
)
c_e_s = pybamm.Variable(
"Separator electrolyte concentration",
domain="separator",
)
c_e_p = pybamm.Variable(
"Positive electrolyte concentration",
domain="positive electrode",
)
# Concatenations combine several variables into a single variable, to simplify
# implementing equations that hold over several domains
c_e = pybamm.Concatenation(c_e_n, c_e_s, c_e_p)
# Electrolyte potential
phi_e_n = pybamm.Variable(
"Negative electrolyte potential",
domain="negative electrode",
)
phi_e_s = pybamm.Variable(
"Separator electrolyte potential",
domain="separator",
)
phi_e_p = pybamm.Variable(
"Positive electrolyte potential",
domain="positive electrode",
)
phi_e = pybamm.Concatenation(phi_e_n, phi_e_s, phi_e_p)
# Electrode potential
phi_s_n = pybamm.Variable(
"Negative electrode potential",
domain="negative electrode",
)
phi_s_p = pybamm.Variable(
"Positive electrode potential",
domain="positive electrode",
)
# Particle concentrations are variables on the particle domain, but also vary in
# the x-direction (electrode domain) and so must be provided with auxiliary
# domains
c_s_n = pybamm.Variable(
"Negative particle concentration",
domain="negative particle",
auxiliary_domains={"secondary": "negative electrode"},
)
c_s_p = pybamm.Variable(
"Positive particle concentration",
domain="positive particle",
auxiliary_domains={"secondary": "positive electrode"},
)
# Constant temperature
T = param.T_init
######################
# Other set-up
######################
# Current density
i_cell = param.current_with_time
# Porosity
# Primary broadcasts are used to broadcast scalar quantities across a domain
# into a vector of the right shape, for multiplying with other vectors
eps_n = pybamm.PrimaryBroadcast(
pybamm.Parameter("Negative electrode porosity"),
"negative electrode")
eps_s = pybamm.PrimaryBroadcast(pybamm.Parameter("Separator porosity"),
"separator")
eps_p = pybamm.PrimaryBroadcast(
pybamm.Parameter("Positive electrode porosity"),
"positive electrode")
eps = pybamm.Concatenation(eps_n, eps_s, eps_p)
# Tortuosity
tor = pybamm.Concatenation(eps_n**param.b_e_n, eps_s**param.b_e_s,
eps_p**param.b_e_p)
# Interfacial reactions
# Surf takes the surface value of a variable, i.e. its boundary value on the
# right side. This is also accessible via `boundary_value(x, "right")`, with
# "left" providing the boundary value of the left side
c_s_surf_n = pybamm.surf(c_s_n)
j0_n = (param.m_n(T) / param.C_r_n * c_e_n**(1 / 2) *
c_s_surf_n**(1 / 2) * (1 - c_s_surf_n)**(1 / 2))
j_n = (2 * j0_n *
pybamm.sinh(param.ne_n / 2 *
(phi_s_n - phi_e_n - param.U_n(c_s_surf_n, T))))
c_s_surf_p = pybamm.surf(c_s_p)
j0_p = (param.gamma_p * param.m_p(T) / param.C_r_p * c_e_p**(1 / 2) *
c_s_surf_p**(1 / 2) * (1 - c_s_surf_p)**(1 / 2))
j_s = pybamm.PrimaryBroadcast(0, "separator")
j_p = (2 * j0_p *
pybamm.sinh(param.ne_p / 2 *
(phi_s_p - phi_e_p - param.U_p(c_s_surf_p, T))))
j = pybamm.Concatenation(j_n, j_s, j_p)
######################
# State of Charge
######################
I = param.dimensional_current_with_time
# The `rhs` dictionary contains differential equations, with the key being the
# variable in the d/dt
self.rhs[Q] = I * param.timescale / 3600
# Initial conditions must be provided for the ODEs
self.initial_conditions[Q] = pybamm.Scalar(0)
######################
# Particles
######################
# The div and grad operators will be converted to the appropriate matrix
# multiplication at the discretisation stage
N_s_n = -param.D_n(c_s_n, T) * pybamm.grad(c_s_n)
N_s_p = -param.D_p(c_s_p, T) * pybamm.grad(c_s_p)
self.rhs[c_s_n] = -(1 / param.C_n) * pybamm.div(N_s_n)
self.rhs[c_s_p] = -(1 / param.C_p) * pybamm.div(N_s_p)
# Boundary conditions must be provided for equations with spatial derivatives
self.boundary_conditions[c_s_n] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
-param.C_n * j_n / param.a_n / param.D_n(c_s_surf_n, T),
"Neumann",
),
}
self.boundary_conditions[c_s_p] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
-param.C_p * j_p / param.a_p / param.gamma_p /
param.D_p(c_s_surf_p, T),
"Neumann",
),
}
# c_n_init and c_p_init can in general be functions of x
# Note the broadcasting, for domains
x_n = pybamm.PrimaryBroadcast(pybamm.standard_spatial_vars.x_n,
"negative particle")
self.initial_conditions[c_s_n] = param.c_n_init(x_n)
x_p = pybamm.PrimaryBroadcast(pybamm.standard_spatial_vars.x_p,
"positive particle")
self.initial_conditions[c_s_p] = param.c_p_init(x_p)
# Events specify points at which a solution should terminate
self.events += [
pybamm.Event(
"Minimum negative particle surface concentration",
pybamm.min(c_s_surf_n) - 0.01,
),
pybamm.Event(
"Maximum negative particle surface concentration",
(1 - 0.01) - pybamm.max(c_s_surf_n),
),
pybamm.Event(
"Minimum positive particle surface concentration",
pybamm.min(c_s_surf_p) - 0.01,
),
pybamm.Event(
"Maximum positive particle surface concentration",
(1 - 0.01) - pybamm.max(c_s_surf_p),
),
]
######################
# Current in the solid
######################
i_s_n = -param.sigma_n * (1 -
eps_n)**param.b_s_n * pybamm.grad(phi_s_n)
sigma_eff_p = param.sigma_p * (1 - eps_p)**param.b_s_p
i_s_p = -sigma_eff_p * pybamm.grad(phi_s_p)
# The `algebraic` dictionary contains differential equations, with the key being
# the main scalar variable of interest in the equation
self.algebraic[phi_s_n] = pybamm.div(i_s_n) + j_n
self.algebraic[phi_s_p] = pybamm.div(i_s_p) + j_p
self.boundary_conditions[phi_s_n] = {
"left": (pybamm.Scalar(0), "Dirichlet"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.boundary_conditions[phi_s_p] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right":
(i_cell / pybamm.boundary_value(-sigma_eff_p, "right"), "Neumann"),
}
# Initial conditions must also be provided for algebraic equations, as an
# initial guess for a root-finding algorithm which calculates consistent initial
# conditions
# We evaluate c_n_init at x=0 and c_p_init at x=1 (this is just an initial
# guess so actual value is not too important)
self.initial_conditions[phi_s_n] = pybamm.Scalar(0)
self.initial_conditions[phi_s_p] = param.U_p(
param.c_p_init(1), param.T_init) - param.U_n(
param.c_n_init(0), param.T_init)
######################
# Current in the electrolyte
######################
i_e = (param.kappa_e(c_e, T) * tor * param.gamma_e / param.C_e) * (
param.chi(c_e) * pybamm.grad(c_e) / c_e - pybamm.grad(phi_e))
self.algebraic[phi_e] = pybamm.div(i_e) - j
self.boundary_conditions[phi_e] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[phi_e] = -param.U_n(param.c_n_init(0),
param.T_init)
######################
# Electrolyte concentration
######################
N_e = -tor * param.D_e(c_e, T) * pybamm.grad(c_e)
self.rhs[c_e] = (1 /
eps) * (-pybamm.div(N_e) / param.C_e +
(1 - param.t_plus(c_e)) * j / param.gamma_e)
self.boundary_conditions[c_e] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[c_e] = param.c_e_init
self.events.append(
pybamm.Event("Zero electrolyte concentration cut-off",
pybamm.min(c_e) - 0.002))
######################
# (Some) variables
######################
voltage = pybamm.boundary_value(phi_s_p, "right")
# The `variables` dictionary contains all variables that might be useful for
# visualising the solution of the model
self.variables = {
"Negative particle surface concentration": c_s_surf_n,
"Electrolyte concentration": c_e,
"Positive particle surface concentration": c_s_surf_p,
"Current [A]": I,
"Negative electrode potential": phi_s_n,
"Electrolyte potential": phi_e,
"Positive electrode potential": phi_s_p,
"Terminal voltage": voltage,
}
self.events += [
pybamm.Event("Minimum voltage", voltage - param.voltage_low_cut),
pybamm.Event("Maximum voltage", voltage - param.voltage_high_cut),
]
def test_max(self):
a = pybamm.StateVector(slice(0, 3))
y_test = np.array([1, 2, 3])
fun = pybamm.max(a)
self.assertIsInstance(fun, pybamm.Function)
self.assertEqual(fun.evaluate(y=y_test), 3)
def test_max(self):
a = pybamm.Vector(np.array([1, 2, 3]))
fun = pybamm.max(a)
self.assertIsInstance(fun, pybamm.Function)
self.assertEqual(fun.evaluate(), 3)
def _get_standard_concentration_variables(
self, c_s, c_s_xav=None, c_s_rav=None, c_s_av=None, c_s_surf=None
):
"""
All particle submodels must provide the particle concentration as an argument
to this method. Some submodels solve for quantities other than the concentration
itself, for example the 'FickianSingleParticle' models solves for the x-averaged
concentration. In such cases the variables being solved for (set in
'get_fundamental_variables') must also be passed as keyword arguments. If not
passed as keyword arguments, the various average concentrations and surface
concentration are computed automatically from the particle concentration.
"""
# Get surface concentration if not provided as fundamental variable to
# solve for
c_s_surf = c_s_surf or pybamm.surf(c_s)
c_s_surf_av = pybamm.x_average(c_s_surf)
if self.domain == "Negative":
c_scale = self.param.c_n_max
elif self.domain == "Positive":
c_scale = self.param.c_p_max
# Get average concentration(s) if not provided as fundamental variable to
# solve for
c_s_xav = c_s_xav or pybamm.x_average(c_s)
c_s_rav = c_s_rav or pybamm.r_average(c_s)
c_s_av = c_s_av or pybamm.r_average(c_s_xav)
variables = {
self.domain + " particle concentration": c_s,
self.domain + " particle concentration [mol.m-3]": c_s * c_scale,
self.domain + " particle concentration [mol.m-3]": c_s * c_scale,
"X-averaged " + self.domain.lower() + " particle concentration": c_s_xav,
"X-averaged "
+ self.domain.lower()
+ " particle concentration [mol.m-3]": c_s_xav * c_scale,
"R-averaged " + self.domain.lower() + " particle concentration": c_s_rav,
"R-averaged "
+ self.domain.lower()
+ " particle concentration [mol.m-3]": c_s_rav * c_scale,
"Average " + self.domain.lower() + " particle concentration": c_s_av,
"Average "
+ self.domain.lower()
+ " particle concentration [mol.m-3]": c_s_av * c_scale,
self.domain + " particle surface concentration": c_s_surf,
self.domain
+ " particle surface concentration [mol.m-3]": c_scale * c_s_surf,
"X-averaged "
+ self.domain.lower()
+ " particle surface concentration": c_s_surf_av,
"X-averaged "
+ self.domain.lower()
+ " particle surface concentration [mol.m-3]": c_scale * c_s_surf_av,
self.domain + " electrode extent of lithiation": c_s_rav,
"X-averaged "
+ self.domain.lower()
+ " electrode extent of lithiation": c_s_av,
"Minimum "
+ self.domain.lower()
+ " particle concentration": pybamm.min(c_s),
"Maximum "
+ self.domain.lower()
+ " particle concentration": pybamm.max(c_s),
"Minimum "
+ self.domain.lower()
+ " particle concentration [mol.m-3]": pybamm.min(c_s) * c_scale,
"Maximum "
+ self.domain.lower()
+ " particle concentration [mol.m-3]": pybamm.max(c_s) * c_scale,
"Minimum "
+ self.domain.lower()
+ " particle surface concentration": pybamm.min(c_s_surf),
"Maximum "
+ self.domain.lower()
+ " particle surface concentration": pybamm.max(c_s_surf),
"Minimum "
+ self.domain.lower()
+ " particle surface concentration [mol.m-3]": pybamm.min(c_s_surf)
* c_scale,
"Maximum "
+ self.domain.lower()
+ " particle surface concentration [mol.m-3]": pybamm.max(c_s_surf)
* c_scale,
}
return variables
def __init__(self, name="Single Particle Model"):
super().__init__({}, name)
pybamm.citations.register("Marquis2019")
# `param` is a class containing all the relevant parameters and functions for
# this model. These are purely symbolic at this stage, and will be set by the
# `ParameterValues` class when the model is processed.
param = self.param
######################
# Variables
######################
# Variables that depend on time only are created without a domain
Q = pybamm.Variable("Discharge capacity [A.h]")
# Variables that vary spatially are created with a domain
c_s_n = pybamm.Variable(
"X-averaged negative particle concentration", domain="negative particle"
)
c_s_p = pybamm.Variable(
"X-averaged positive particle concentration", domain="positive particle"
)
# Constant temperature
T = param.T_init
######################
# Other set-up
######################
# Current density
i_cell = param.current_with_time
j_n = i_cell / param.l_n
j_p = -i_cell / param.l_p
######################
# State of Charge
######################
I = param.dimensional_current_with_time
# The `rhs` dictionary contains differential equations, with the key being the
# variable in the d/dt
self.rhs[Q] = I * param.timescale / 3600
# Initial conditions must be provided for the ODEs
self.initial_conditions[Q] = pybamm.Scalar(0)
######################
# Particles
######################
# The div and grad operators will be converted to the appropriate matrix
# multiplication at the discretisation stage
N_s_n = -param.D_n(c_s_n, T) * pybamm.grad(c_s_n)
N_s_p = -param.D_p(c_s_p, T) * pybamm.grad(c_s_p)
self.rhs[c_s_n] = -(1 / param.C_n) * pybamm.div(N_s_n)
self.rhs[c_s_p] = -(1 / param.C_p) * pybamm.div(N_s_p)
# Surf takes the surface value of a variable, i.e. its boundary value on the
# right side. This is also accessible via `boundary_value(x, "right")`, with
# "left" providing the boundary value of the left side
c_s_surf_n = pybamm.surf(c_s_n)
c_s_surf_p = pybamm.surf(c_s_p)
# Boundary conditions must be provided for equations with spatial derivatives
self.boundary_conditions[c_s_n] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
-param.C_n * j_n / param.a_R_n / param.D_n(c_s_surf_n, T),
"Neumann",
),
}
self.boundary_conditions[c_s_p] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
-param.C_p
* j_p
/ param.a_R_p
/ param.gamma_p
/ param.D_p(c_s_surf_p, T),
"Neumann",
),
}
# c_n_init and c_p_init are functions, but for the SPM we evaluate them at x=0
# and x=1 since there is no x-dependence in the particles
self.initial_conditions[c_s_n] = param.c_n_init(0)
self.initial_conditions[c_s_p] = param.c_p_init(1)
# Events specify points at which a solution should terminate
self.events += [
pybamm.Event(
"Minimum negative particle surface concentration",
pybamm.min(c_s_surf_n) - 0.01,
),
pybamm.Event(
"Maximum negative particle surface concentration",
(1 - 0.01) - pybamm.max(c_s_surf_n),
),
pybamm.Event(
"Minimum positive particle surface concentration",
pybamm.min(c_s_surf_p) - 0.01,
),
pybamm.Event(
"Maximum positive particle surface concentration",
(1 - 0.01) - pybamm.max(c_s_surf_p),
),
]
# Note that the SPM does not have any algebraic equations, so the `algebraic`
# dictionary remains empty
######################
# (Some) variables
######################
# Interfacial reactions
j0_n = param.j0_n(1, c_s_surf_n, T) / param.C_r_n
j0_p = param.gamma_p * param.j0_p(1, c_s_surf_p, T) / param.C_r_p
eta_n = (2 / param.ne_n) * pybamm.arcsinh(j_n / (2 * j0_n))
eta_p = (2 / param.ne_p) * pybamm.arcsinh(j_p / (2 * j0_p))
phi_s_n = 0
phi_e = -eta_n - param.U_n(c_s_surf_n, T)
phi_s_p = eta_p + phi_e + param.U_p(c_s_surf_p, T)
V = phi_s_p
whole_cell = ["negative electrode", "separator", "positive electrode"]
# The `variables` dictionary contains all variables that might be useful for
# visualising the solution of the model
# Primary broadcasts are used to broadcast scalar quantities across a domain
# into a vector of the right shape, for multiplying with other vectors
self.variables = {
"Negative particle surface concentration": pybamm.PrimaryBroadcast(
c_s_surf_n, "negative electrode"
),
"Electrolyte concentration": pybamm.PrimaryBroadcast(1, whole_cell),
"Positive particle surface concentration": pybamm.PrimaryBroadcast(
c_s_surf_p, "positive electrode"
),
"Current [A]": I,
"Negative electrode potential": pybamm.PrimaryBroadcast(
phi_s_n, "negative electrode"
),
"Electrolyte potential": pybamm.PrimaryBroadcast(phi_e, whole_cell),
"Positive electrode potential": pybamm.PrimaryBroadcast(
phi_s_p, "positive electrode"
),
"Terminal voltage": V,
}
self.events += [
pybamm.Event("Minimum voltage", V - param.voltage_low_cut),
pybamm.Event("Maximum voltage", V - param.voltage_high_cut),
]
def __init__(self, name="Basic full model"):
super().__init__({}, name)
# `param` is a class containing all the relevant parameters and functions for
# this model. These are purely symbolic at this stage, and will be set by the
# `ParameterValues` class when the model is processed.
param = self.param
######################
# Variables
######################
# Variables that depend on time only are created without a domain
Q = pybamm.Variable("Discharge capacity [A.h]")
# Variables that vary spatially are created with a domain
c_e_n = pybamm.Variable(
"Negative electrolyte concentration",
domain="negative electrode",
)
c_e_s = pybamm.Variable(
"Separator electrolyte concentration",
domain="separator",
)
c_e_p = pybamm.Variable(
"Positive electrolyte concentration",
domain="positive electrode",
)
# Concatenations combine several variables into a single variable, to simplify
# implementing equations that hold over several domains
c_e = pybamm.Concatenation(c_e_n, c_e_s, c_e_p)
# Electrolyte potential
phi_e_n = pybamm.Variable(
"Negative electrolyte potential",
domain="negative electrode",
)
phi_e_s = pybamm.Variable(
"Separator electrolyte potential",
domain="separator",
)
phi_e_p = pybamm.Variable(
"Positive electrolyte potential",
domain="positive electrode",
)
phi_e = pybamm.Concatenation(phi_e_n, phi_e_s, phi_e_p)
# Electrode potential
phi_s_n = pybamm.Variable(
"Negative electrode potential",
domain="negative electrode",
)
phi_s_p = pybamm.Variable(
"Positive electrode potential",
domain="positive electrode",
)
# Porosity
eps_n = pybamm.Variable(
"Negative electrode porosity",
domain="negative electrode",
)
eps_s = pybamm.Variable("Separator porosity", domain="separator")
eps_p = pybamm.Variable(
"Positive electrode porosity",
domain="positive electrode",
)
eps = pybamm.Concatenation(eps_n, eps_s, eps_p)
# Pressure (for convection)
pressure_n = pybamm.Variable(
"Negative electrolyte pressure",
domain="negative electrode",
)
pressure_p = pybamm.Variable(
"Positive electrolyte pressure",
domain="positive electrode",
)
# Constant temperature
T = param.T_init
######################
# Other set-up
######################
# Current density
i_cell = param.current_with_time
# Tortuosity
tor = pybamm.Concatenation(eps_n**param.b_e_n, eps_s**param.b_e_s,
eps_p**param.b_e_p)
# Interfacial reactions
j0_n = param.j0_n(c_e_n, T)
j_n = (2 * j0_n *
pybamm.sinh(param.ne_n / 2 *
(phi_s_n - phi_e_n - param.U_n(c_e_n, T))))
j0_p = param.j0_p(c_e_p, T)
j_s = pybamm.PrimaryBroadcast(0, "separator")
j_p = (2 * j0_p *
pybamm.sinh(param.ne_p / 2 *
(phi_s_p - phi_e_p - param.U_p(c_e_p, T))))
j = pybamm.Concatenation(j_n, j_s, j_p)
######################
# State of Charge
######################
I = param.dimensional_current_with_time
# The `rhs` dictionary contains differential equations, with the key being the
# variable in the d/dt
self.rhs[Q] = I * param.timescale / 3600
# Initial conditions must be provided for the ODEs
self.initial_conditions[Q] = pybamm.Scalar(0)
######################
# Convection
######################
v_n = -pybamm.grad(pressure_n)
v_p = -pybamm.grad(pressure_p)
l_s = pybamm.geometric_parameters.l_s
l_n = pybamm.geometric_parameters.l_n
x_s = pybamm.SpatialVariable("x_s", domain="separator")
# Difference in negative and positive electrode velocities determines the
# velocity in the separator
v_n_right = param.beta_n * i_cell
v_p_left = param.beta_p * i_cell
d_v_s__dx = (v_p_left - v_n_right) / l_s
# Simple formula for velocity in the separator
div_V_s = -d_v_s__dx
v_s = d_v_s__dx * (x_s - l_n) + v_n_right
# v is the velocity in the x-direction
# div_V is the divergence of the velocity in the yz-directions
v = pybamm.Concatenation(v_n, v_s, v_p)
div_V = pybamm.Concatenation(
pybamm.PrimaryBroadcast(0, "negative electrode"),
pybamm.PrimaryBroadcast(div_V_s, "separator"),
pybamm.PrimaryBroadcast(0, "positive electrode"),
)
# Simple formula for velocity in the separator
self.algebraic[pressure_n] = pybamm.div(v_n) - param.beta_n * j_n
self.algebraic[pressure_p] = pybamm.div(v_p) - param.beta_p * j_p
self.boundary_conditions[pressure_n] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (pybamm.Scalar(0), "Dirichlet"),
}
self.boundary_conditions[pressure_p] = {
"left": (pybamm.Scalar(0), "Dirichlet"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[pressure_n] = pybamm.Scalar(0)
self.initial_conditions[pressure_p] = pybamm.Scalar(0)
######################
# Current in the electrolyte
######################
i_e = (param.kappa_e(c_e, T) * tor * param.gamma_e / param.C_e) * (
param.chi(c_e) * pybamm.grad(c_e) / c_e - pybamm.grad(phi_e))
self.algebraic[phi_e] = pybamm.div(i_e) - j
self.boundary_conditions[phi_e] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[phi_e] = -param.U_n(param.c_e_init,
param.T_init)
######################
# Current in the solid
######################
i_s_n = -param.sigma_n * (1 -
eps_n)**param.b_s_n * pybamm.grad(phi_s_n)
sigma_eff_p = param.sigma_p * (1 - eps_p)**param.b_s_p
i_s_p = -sigma_eff_p * pybamm.grad(phi_s_p)
# The `algebraic` dictionary contains differential equations, with the key being
# the main scalar variable of interest in the equation
self.algebraic[phi_s_n] = pybamm.div(i_s_n) + j_n
self.algebraic[phi_s_p] = pybamm.div(i_s_p) + j_p
self.boundary_conditions[phi_s_n] = {
"left": (pybamm.Scalar(0), "Dirichlet"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.boundary_conditions[phi_s_p] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right":
(i_cell / pybamm.boundary_value(-sigma_eff_p, "right"), "Neumann"),
}
# Initial conditions must also be provided for algebraic equations, as an
# initial guess for a root-finding algorithm which calculates consistent initial
# conditions
self.initial_conditions[phi_s_n] = pybamm.Scalar(0)
self.initial_conditions[phi_s_p] = param.U_p(
param.c_e_init, param.T_init) - param.U_n(param.c_e_init,
param.T_init)
######################
# Porosity
######################
beta_surf = pybamm.Concatenation(
pybamm.PrimaryBroadcast(param.beta_surf_n, "negative electrode"),
pybamm.PrimaryBroadcast(0, "separator"),
pybamm.PrimaryBroadcast(param.beta_surf_p, "positive electrode"),
)
deps_dt = -beta_surf * j
self.rhs[eps] = deps_dt
self.initial_conditions[eps] = param.epsilon_init
self.events.extend([
pybamm.Event("Zero negative electrode porosity cut-off",
pybamm.min(eps_n)),
pybamm.Event("Max negative electrode porosity cut-off",
pybamm.max(eps_n) - 1),
pybamm.Event("Zero positive electrode porosity cut-off",
pybamm.min(eps_p)),
pybamm.Event("Max positive electrode porosity cut-off",
pybamm.max(eps_p) - 1),
])
######################
# Electrolyte concentration
######################
N_e = (-tor * param.D_e(c_e, T) * pybamm.grad(c_e) +
param.C_e * param.t_plus(c_e) * i_e / param.gamma_e +
param.C_e * c_e * v)
s = pybamm.Concatenation(
pybamm.PrimaryBroadcast(param.s_plus_n_S, "negative electrode"),
pybamm.PrimaryBroadcast(0, "separator"),
pybamm.PrimaryBroadcast(param.s_plus_p_S, "positive electrode"),
)
self.rhs[c_e] = (1 / eps) * (-pybamm.div(N_e) / param.C_e +
s * j / param.gamma_e - c_e * deps_dt -
c_e * div_V)
self.boundary_conditions[c_e] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[c_e] = param.c_e_init
self.events.append(
pybamm.Event("Zero electrolyte concentration cut-off",
pybamm.min(c_e) - 0.002))
######################
# (Some) variables
######################
voltage = pybamm.boundary_value(phi_s_p, "right")
# The `variables` dictionary contains all variables that might be useful for
# visualising the solution of the model
pot = param.potential_scale
self.variables = {
"Electrolyte concentration":
c_e,
"Current [A]":
I,
"Negative electrode potential [V]":
pot * phi_s_n,
"Electrolyte potential [V]":
-param.U_n_ref + pot * phi_e,
"Positive electrode potential [V]":
param.U_p_ref - param.U_n_ref + pot * phi_s_p,
"Terminal voltage [V]":
param.U_p_ref - param.U_n_ref + pot * voltage,
"x [m]":
pybamm.standard_spatial_vars.x * param.L_x,
"x":
pybamm.standard_spatial_vars.x,
"Porosity":
eps,
"Volume-averaged velocity":
v,
"X-averaged separator transverse volume-averaged velocity":
div_V_s,
}
self.events.extend([
pybamm.Event("Minimum voltage", voltage - param.voltage_low_cut),
pybamm.Event("Maximum voltage", voltage - param.voltage_high_cut),
])
def __init__(self, name="Doyle-Fuller-Newman half cell model", options=None):
super().__init__({}, name)
pybamm.citations.register("Marquis2019")
# `param` is a class containing all the relevant parameters and functions for
# this model. These are purely symbolic at this stage, and will be set by the
# `ParameterValues` class when the model is processed.
param = self.param
options = options or {"working electrode": None}
if options["working electrode"] not in ["negative", "positive"]:
raise ValueError(
"The option 'working electrode' should be either 'positive'"
" or 'negative'"
)
self.options.update(options)
working_electrode = options["working electrode"]
if working_electrode == "negative":
R_w_typ = param.R_n_typ
else:
R_w_typ = param.R_p_typ
# Set default length scales
self.length_scales = {
"working electrode": param.L_x,
"separator": param.L_x,
"working particle": R_w_typ,
"current collector y": param.L_z,
"current collector z": param.L_z,
}
######################
# Variables
######################
# Variables that depend on time only are created without a domain
Q = pybamm.Variable("Discharge capacity [A.h]")
# Define some useful scalings
pot = param.potential_scale
i_typ = param.current_scale
# Variables that vary spatially are created with a domain.
c_e_s = pybamm.Variable(
"Separator electrolyte concentration", domain="separator"
)
c_e_w = pybamm.Variable(
"Working electrolyte concentration", domain="working electrode"
)
c_e = pybamm.concatenation(c_e_s, c_e_w)
c_s_w = pybamm.Variable(
"Working particle concentration",
domain="working particle",
auxiliary_domains={"secondary": "working electrode"},
)
phi_s_w = pybamm.Variable(
"Working electrode potential", domain="working electrode"
)
phi_e_s = pybamm.Variable("Separator electrolyte potential", domain="separator")
phi_e_w = pybamm.Variable(
"Working electrolyte potential", domain="working electrode"
)
phi_e = pybamm.concatenation(phi_e_s, phi_e_w)
# Constant temperature
T = param.T_init
######################
# Other set-up
######################
# Current density
i_cell = param.current_with_time
# Define particle surface concentration
# Surf takes the surface value of a variable, i.e. its boundary value on the
# right side. This is also accessible via `boundary_value(x, "right")`, with
# "left" providing the boundary value of the left side
c_s_surf_w = pybamm.surf(c_s_w)
# Define parameters. We need to assemble them differently depending on the
# working electrode
if working_electrode == "negative":
# Porosity and Tortuosity
# Primary broadcasts are used to broadcast scalar quantities across a domain
# into a vector of the right shape, for multiplying with other vectors
eps_s = pybamm.PrimaryBroadcast(
pybamm.Parameter("Separator porosity"), "separator"
)
eps_w = pybamm.PrimaryBroadcast(
pybamm.Parameter("Negative electrode porosity"), "working electrode"
)
b_e_s = param.b_e_s
b_e_w = param.b_e_n
# Interfacial reactions
j0_w = param.j0_n(c_e_w, c_s_surf_w, T) / param.C_r_n
U_w = param.U_n
ne_w = param.ne_n
# Particle diffusion parameters
D_w = param.D_n
C_w = param.C_n
a_R_w = param.a_R_n
gamma_w = pybamm.Scalar(1)
c_w_init = param.c_n_init
# Electrode equation parameters
eps_s_w = pybamm.Parameter(
"Negative electrode active material volume fraction"
)
b_s_w = param.b_s_n
sigma_w = param.sigma_n
# Other parameters (for outputs)
c_w_max = param.c_n_max
U_ref = param.U_n_ref
phi_s_w_ref = pybamm.Scalar(0)
L_w = param.L_n
else:
# Porosity and Tortuosity
eps_s = pybamm.PrimaryBroadcast(
pybamm.Parameter("Separator porosity"), "separator"
)
eps_w = pybamm.PrimaryBroadcast(
pybamm.Parameter("Positive electrode porosity"), "working electrode"
)
b_e_s = param.b_e_s
b_e_w = param.b_e_p
# Interfacial reactions
j0_w = param.gamma_p * param.j0_p(c_e_w, c_s_surf_w, T) / param.C_r_p
U_w = param.U_p
ne_w = param.ne_p
# Particle diffusion parameters
D_w = param.D_p
C_w = param.C_p
a_R_w = param.a_R_p
gamma_w = param.gamma_p
c_w_init = param.c_p_init
# Electrode equation parameters
eps_s_w = pybamm.Parameter(
"Positive electrode active material volume fraction"
)
b_s_w = param.b_s_p
sigma_w = param.sigma_p
# Other parameters (for outputs)
c_w_max = param.c_p_max
U_ref = param.U_p_ref
phi_s_w_ref = param.U_p_ref - param.U_n_ref
L_w = param.L_p
eps = pybamm.concatenation(eps_s, eps_w)
tor = pybamm.concatenation(eps_s ** b_e_s, eps_w ** b_e_w)
j_w = (
2 * j0_w * pybamm.sinh(ne_w / 2 * (phi_s_w - phi_e_w - U_w(c_s_surf_w, T)))
)
j_s = pybamm.PrimaryBroadcast(0, "separator")
j = pybamm.concatenation(j_s, j_w)
######################
# State of Charge
######################
I = param.dimensional_current_with_time
# The `rhs` dictionary contains differential equations, with the key being the
# variable in the d/dt
self.rhs[Q] = I * param.timescale / 3600
# Initial conditions must be provided for the ODEs
self.initial_conditions[Q] = pybamm.Scalar(0)
######################
# Particles
######################
# The div and grad operators will be converted to the appropriate matrix
# multiplication at the discretisation stage
N_s_w = -D_w(c_s_w, T) * pybamm.grad(c_s_w)
self.rhs[c_s_w] = -(1 / C_w) * pybamm.div(N_s_w)
# Boundary conditions must be provided for equations with spatial
# derivatives
self.boundary_conditions[c_s_w] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
-C_w * j_w / a_R_w / gamma_w / D_w(c_s_surf_w, T),
"Neumann",
),
}
# c_w_init can in general be a function of x
# Note the broadcasting, for domains
x_w = pybamm.PrimaryBroadcast(half_cell_spatial_vars.x_w, "working particle")
self.initial_conditions[c_s_w] = c_w_init(x_w)
# Events specify points at which a solution should terminate
self.events += [
pybamm.Event(
"Minimum working particle surface concentration",
pybamm.min(c_s_surf_w) - 0.01,
),
pybamm.Event(
"Maximum working particle surface concentration",
(1 - 0.01) - pybamm.max(c_s_surf_w),
),
]
######################
# Current in the solid
######################
sigma_eff_w = sigma_w * eps_s_w ** b_s_w
i_s_w = -sigma_eff_w * pybamm.grad(phi_s_w)
self.boundary_conditions[phi_s_w] = {
"left": (pybamm.Scalar(0), "Neumann"),
"right": (
i_cell / pybamm.boundary_value(-sigma_eff_w, "right"),
"Neumann",
),
}
self.algebraic[phi_s_w] = pybamm.div(i_s_w) + j_w
# Initial conditions must also be provided for algebraic equations, as an
# initial guess for a root-finding algorithm which calculates consistent
# initial conditions
self.initial_conditions[phi_s_w] = U_w(c_w_init(1), param.T_init)
######################
# Electrolyte concentration
######################
N_e = -tor * param.D_e(c_e, T) * pybamm.grad(c_e)
self.rhs[c_e] = (1 / eps) * (
-pybamm.div(N_e) / param.C_e
+ (1 - param.t_plus(c_e, T)) * j / param.gamma_e
)
dce_dx = (
-(1 - param.t_plus(c_e, T))
* i_cell
* param.C_e
/ (tor * param.gamma_e * param.D_e(c_e, T))
)
self.boundary_conditions[c_e] = {
"left": (pybamm.boundary_value(dce_dx, "left"), "Neumann"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[c_e] = param.c_e_init
self.events.append(
pybamm.Event(
"Zero electrolyte concentration cut-off", pybamm.min(c_e) - 0.002
)
)
######################
# Current in the electrolyte
######################
i_e = (param.kappa_e(c_e, T) * tor * param.gamma_e / param.C_e) * (
param.chi(c_e, T) * pybamm.grad(c_e) / c_e - pybamm.grad(phi_e)
)
self.algebraic[phi_e] = pybamm.div(i_e) - j
ref_potential = param.U_n_ref / pot
self.boundary_conditions[phi_e] = {
"left": (ref_potential, "Dirichlet"),
"right": (pybamm.Scalar(0), "Neumann"),
}
self.initial_conditions[phi_e] = ref_potential
######################
# (Some) variables
######################
L_Li = pybamm.Parameter("Lithium counter electrode thickness [m]")
sigma_Li = pybamm.Parameter("Lithium counter electrode conductivity [S.m-1]")
j_Li = pybamm.Parameter(
"Lithium counter electrode exchange-current density [A.m-2]"
)
vdrop_cell = pybamm.boundary_value(phi_s_w, "right") - ref_potential
vdrop_Li = -(
2 * pybamm.arcsinh(i_cell * i_typ / j_Li)
+ L_Li * i_typ * i_cell / (sigma_Li * pot)
)
voltage = vdrop_cell + vdrop_Li
c_e_total = pybamm.x_average(eps * c_e)
c_s_surf_w_av = pybamm.x_average(c_s_surf_w)
c_s_rav = pybamm.r_average(c_s_w)
c_s_vol_av = pybamm.x_average(eps_s_w * c_s_rav)
# The `variables` dictionary contains all variables that might be useful for
# visualising the solution of the model
self.variables = {
"Time [s]": param.timescale * pybamm.t,
"Working particle surface concentration": c_s_surf_w,
"X-averaged working particle surface concentration": c_s_surf_w_av,
"Working particle concentration": c_s_w,
"Working particle surface concentration [mol.m-3]": c_w_max * c_s_surf_w,
"X-averaged working particle surface concentration "
"[mol.m-3]": c_w_max * c_s_surf_w_av,
"Working particle concentration [mol.m-3]": c_w_max * c_s_w,
"Total lithium in working electrode": c_s_vol_av,
"Total lithium in working electrode [mol]": c_s_vol_av
* c_w_max
* L_w
* param.A_cc,
"Electrolyte concentration": c_e,
"Electrolyte concentration [mol.m-3]": param.c_e_typ * c_e,
"Total electrolyte concentration": c_e_total,
"Total electrolyte concentration [mol]": c_e_total
* param.c_e_typ
* L_w
* param.L_s
* param.A_cc,
"Current [A]": I,
"Working electrode potential": phi_s_w,
"Working electrode potential [V]": phi_s_w_ref + pot * phi_s_w,
"Working electrode open circuit potential": U_w(c_s_surf_w, T),
"Working electrode open circuit potential [V]": U_ref
+ pot * U_w(c_s_surf_w, T),
"Electrolyte potential": phi_e,
"Electrolyte potential [V]": -param.U_n_ref + pot * phi_e,
"Voltage drop in the cell": vdrop_cell,
"Voltage drop in the cell [V]": phi_s_w_ref
+ param.U_n_ref
+ pot * vdrop_cell,
"Terminal voltage": voltage,
"Terminal voltage [V]": phi_s_w_ref + param.U_n_ref + pot * voltage,
}
