Files
SystemSimulationApp/PythonModels/components/resistive_pipe.py
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4.5 KiB
Python

from __future__ import annotations
from collections.abc import Mapping
from math import pi
from PythonModels.core.base import AlgebraicComponent
from PythonModels.core.equations import EquationResidual
from PythonModels.core.metadata import ParameterDefinition
from PythonModels.core.medium import IdealGasMedium
from PythonModels.core.ports import PortDefinition
class ResistivePipe(AlgebraicComponent):
"""Quasi-steady Darcy resistance used by topology-driven simulation."""
MODEL_TYPE = "pipe"
PORTS = (
PortDefinition.pneumatic("port_a", nominal_role="inlet"),
PortDefinition.pneumatic("port_b", nominal_role="outlet"),
)
PARAMETERS = (
ParameterDefinition(
"length",
5.0,
label="长度",
quantity="length",
unit="m",
minimum=0.0,
minimum_exclusive=True,
),
ParameterDefinition(
"diameter",
0.02,
label="直径",
quantity="length",
unit="m",
minimum=0.0,
minimum_exclusive=True,
),
ParameterDefinition(
"lambda_darcy",
0.02,
label="摩阻系数",
minimum=0.0,
),
ParameterDefinition(
"p0",
1e5,
label="初始压力",
quantity="pressure",
unit="Pa",
minimum=0.0,
minimum_exclusive=True,
),
ParameterDefinition(
"T0",
300.0,
label="初始温度",
quantity="temperature",
unit="K",
minimum=0.0,
minimum_exclusive=True,
),
)
RESULT_VARIABLES = ()
def __init__(
self,
name: str,
medium: IdealGasMedium,
L: float = 5.0,
D: float = 0.02,
lambda_darcy: float = 0.02,
p0: float = 1e5,
T0: float = 300.0,
) -> None:
super().__init__(name=name)
self.set_parameter_values(
{
"length": L,
"diameter": D,
"lambda_darcy": lambda_darcy,
"p0": p0,
"T0": T0,
}
)
self.medium = medium
self.L = L
self.D = D
self.lambda_darcy = lambda_darcy
self.p0 = p0
self.T0 = T0
self.area = pi * D * D / 4.0
initial_h = medium.specific_enthalpy(T0)
self.port_a = self.register_declared_port("port_a")
self.port_a.p = p0
self.port_a.h_outflow = initial_h
self.port_b = self.register_declared_port("port_b")
self.port_b.p = p0
self.port_b.h_outflow = initial_h
def pressure_drop(self, m_flow_a: float, p_a: float, p_b: float) -> float:
average_pressure = max(0.5 * (p_a + p_b), 1.0)
density = max(self.medium.density(average_pressure, self.T0), 1e-12)
resistance = self.lambda_darcy * (self.L / self.D)
return (
resistance
* m_flow_a
* abs(m_flow_a)
/ (2.0 * density * self.area * self.area)
)
def pressure_flow_equation_residuals(self) -> tuple[EquationResidual, ...]:
return (
EquationResidual(
id=f"{self.name}:mass_flow_balance",
owner="component",
owner_id=self.name,
relation="sumToZero",
variables=(
f"{self.name}.port_a.m_flow",
f"{self.name}.port_b.m_flow",
),
role="flow",
value=self.port_a.m_flow + self.port_b.m_flow,
),
EquationResidual(
id=f"{self.name}:darcy_pressure_loss",
owner="component",
owner_id=self.name,
relation="constitutive",
variables=(
f"{self.name}.port_a.p",
f"{self.name}.port_b.p",
f"{self.name}.port_a.m_flow",
),
role="effort",
value=(
self.port_a.p
- self.port_b.p
- self.pressure_drop(
self.port_a.m_flow,
self.port_a.p,
self.port_b.p,
)
),
),
)
def update_stream_outflows(self, connected_h: Mapping[str, float]) -> None:
self.port_a.h_outflow = connected_h["port_b"]
self.port_b.h_outflow = connected_h["port_a"]