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pybamm/models/full_battery_models/lithium_ion/basic_reservoir.py
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# | ||
# Basic Reservoir Model | ||
# | ||
import pybamm | ||
from .base_lithium_ion_model import BaseModel | ||
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class BasicReservoir(BaseModel): | ||
"""Reservoir model of a lithium-ion battery, from | ||
:footcite:t:`Marquis2019`. | ||
Parameters | ||
---------- | ||
name : str, optional | ||
The name of the model. | ||
""" | ||
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def __init__(self, name="Reservoir 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 | ||
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###################### | ||
# 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 | ||
sto_n = pybamm.Variable( | ||
"Average negative particle stoichiometry", | ||
domain="current collector", | ||
bounds=(0, 1), | ||
) | ||
sto_p = pybamm.Variable( | ||
"Average positive particle stoichiometry", | ||
domain="current collector", | ||
bounds=(0, 1), | ||
) | ||
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# Constant temperature | ||
T = param.T_init | ||
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###################### | ||
# Other set-up | ||
###################### | ||
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# Current density | ||
i_cell = param.current_density_with_time | ||
a_n = 3 * param.n.prim.epsilon_s_av / param.n.prim.R_typ | ||
a_p = 3 * param.p.prim.epsilon_s_av / param.p.prim.R_typ | ||
j_n = i_cell / (param.n.L * a_n) | ||
j_p = -i_cell / (param.p.L * a_p) | ||
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###################### | ||
# State of Charge | ||
###################### | ||
I = param.current_with_time | ||
# The `rhs` dictionary contains differential equations, with the key being the | ||
# variable in the d/dt | ||
self.rhs[Q] = I / 3600 | ||
# Initial conditions must be provided for the ODEs | ||
self.initial_conditions[Q] = pybamm.Scalar(0) | ||
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###################### | ||
# Particles | ||
###################### | ||
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self.rhs[sto_n] = -i_cell / ( | ||
param.n.L * param.n.prim.epsilon_s_av * param.n.prim.c_max * param.F | ||
) | ||
self.rhs[sto_p] = i_cell / ( | ||
param.p.L * param.p.prim.epsilon_s_av * param.p.prim.c_max * param.F | ||
) | ||
# c_n_init and c_p_init are functions of r and x, but for the reservoir model | ||
# we take the x-averaged and r-averaged value since there are no x-dependence | ||
# nor r-dependencein the particles | ||
self.initial_conditions[sto_n] = ( | ||
pybamm.x_average(pybamm.r_average(param.n.prim.c_init)) / param.n.prim.c_max | ||
) | ||
self.initial_conditions[sto_p] = ( | ||
pybamm.x_average(pybamm.r_average(param.p.prim.c_init)) / param.p.prim.c_max | ||
) | ||
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self.events += [ | ||
pybamm.Event( | ||
"Minimum negative particle surface stoichiometry", | ||
sto_n - 0.01, | ||
), | ||
pybamm.Event( | ||
"Maximum negative particle surface stoichiometry", | ||
(1 - 0.01) - sto_n, | ||
), | ||
pybamm.Event( | ||
"Minimum positive particle surface stoichiometry", | ||
sto_p - 0.01, | ||
), | ||
pybamm.Event( | ||
"Maximum positive particle surface stoichiometry", | ||
(1 - 0.01) - sto_p, | ||
), | ||
] | ||
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# Note that the reservoir model does not have any algebraic equations, so the | ||
# `algebraic` dictionary remains empty | ||
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###################### | ||
# (Some) variables | ||
###################### | ||
# Interfacial reactions | ||
RT_F = param.R * T / param.F | ||
j0_n = param.n.prim.j0(param.c_e_init_av, sto_n * param.n.prim.c_max, T) | ||
j0_p = param.p.prim.j0(param.c_e_init_av, sto_p * param.p.prim.c_max, T) | ||
eta_n = (2 / param.n.prim.ne) * RT_F * pybamm.arcsinh(j_n / (2 * j0_n)) | ||
eta_p = (2 / param.p.prim.ne) * RT_F * pybamm.arcsinh(j_p / (2 * j0_p)) | ||
phi_s_n = 0 | ||
phi_e = -eta_n - param.n.prim.U(sto_n, T) | ||
phi_s_p = eta_p + phi_e + param.p.prim.U(sto_p, T) | ||
V = phi_s_p | ||
num_cells = pybamm.Parameter( | ||
"Number of cells connected in series to make a battery" | ||
) | ||
c_s_n = sto_n * param.n.prim.c_max | ||
c_s_p = sto_p * param.p.prim.c_max | ||
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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 = { | ||
"Time [s]": pybamm.t, | ||
"Discharge capacity [A.h]": Q, | ||
"X-averaged negative particle concentration [mol.m-3]": pybamm.PrimaryBroadcast( | ||
c_s_n, "negative particle" | ||
), | ||
"Negative particle surface " | ||
"concentration [mol.m-3]": pybamm.PrimaryBroadcast( | ||
c_s_n, "negative electrode" | ||
), | ||
"Electrolyte concentration [mol.m-3]": pybamm.PrimaryBroadcast( | ||
param.c_e_init_av, whole_cell | ||
), | ||
"X-averaged positive particle concentration [mol.m-3]": pybamm.PrimaryBroadcast( | ||
c_s_p, "positive particle" | ||
), | ||
"Positive particle surface " | ||
"concentration [mol.m-3]": pybamm.PrimaryBroadcast( | ||
c_s_p, "positive electrode" | ||
), | ||
"Current [A]": I, | ||
"Current variable [A]": I, # for compatibility with pybamm.Experiment | ||
"Negative electrode potential [V]": pybamm.PrimaryBroadcast( | ||
phi_s_n, "negative electrode" | ||
), | ||
"Electrolyte potential [V]": pybamm.PrimaryBroadcast(phi_e, whole_cell), | ||
"Positive electrode potential [V]": pybamm.PrimaryBroadcast( | ||
phi_s_p, "positive electrode" | ||
), | ||
"Voltage [V]": V, | ||
"Battery voltage [V]": V * num_cells, | ||
} | ||
# Events specify points at which a solution should terminate | ||
self.events += [ | ||
pybamm.Event("Minimum voltage [V]", V - param.voltage_low_cut), | ||
pybamm.Event("Maximum voltage [V]", param.voltage_high_cut - V), | ||
] |
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