Replace Python numerical kernels with native C execution

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ljz committed 2026-09-10 01:12:18 +08:00
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"""Component parameters, ports and output definitions; numerical equations execute in C."""
from __future__ import annotations
from collections.abc import Mapping
from app.simulation.core.base import ThermodynamicVolumeComponent
from app.simulation.core.catalog import ComponentDisplaySpec, PortDisplaySpec
from app.simulation.core.equations import EquationResidual
from app.simulation.core.metadata import (
ParameterDefinition,
THERMODYNAMIC_VOLUME_RESULT_VARIABLES,
)
from app.simulation.core.medium import IdealGasMedium, ThermodynamicProperties
from app.simulation.core.metadata import ParameterDefinition, THERMODYNAMIC_VOLUME_RESULT_VARIABLES
from app.simulation.core.medium import IdealGasMedium
from app.simulation.core.ports import PortDefinition
from app.simulation.core.state import VolumeState
class Tank(ThermodynamicVolumeComponent):
"""Python port of ModelicaModels.Mytank."""
MODEL_TYPE = "tank"
MODEL_VERSION = "1.0.0"
PORTS = (PortDefinition.pneumatic("port_a", nominal_role="inlet"),)
PARAMETERS = (
ParameterDefinition(
"volume",
0.1,
label="容积",
quantity="volume",
unit="m3",
minimum=0.0,
minimum_exclusive=True,
),
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,
),
)
MODEL_TYPE = 'tank'
MODEL_VERSION = '1.0.0'
PORTS = (PortDefinition.pneumatic('port_a', nominal_role='inlet'),)
PARAMETERS = (ParameterDefinition('volume', 0.1, label='容积', quantity='volume', unit='m3', minimum=0.0, minimum_exclusive=True), ParameterDefinition('p0', 100000.0, 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 = THERMODYNAMIC_VOLUME_RESULT_VARIABLES
DISPLAY = ComponentDisplaySpec(
label="贮箱",
library_id="experimental",
category_id="storage",
symbol="tank",
ports=(PortDisplaySpec("port_a", "left"),),
order=20,
)
DISPLAY = ComponentDisplaySpec(label='贮箱', library_id='experimental', category_id='storage', symbol='tank', ports=(PortDisplaySpec('port_a', 'left'),), order=20)
def __init__(
self,
name: str,
medium: IdealGasMedium,
V: float = 0.1,
p0: float = 1e5,
T0: float = 300.0,
) -> None:
def __init__(self, name: str, medium: IdealGasMedium, V: float=0.1, p0: float=100000.0, T0: float=300.0) -> None:
super().__init__(name=name)
self.set_parameter_values({"volume": V, "p0": p0, "T0": T0})
self.set_parameter_values({'volume': V, 'p0': p0, 'T0': T0})
self.medium = medium
self.V = V
m0 = p0 * V / (medium.R_gas * T0)
U0 = m0 * medium.specific_internal_energy(T0)
self.state = VolumeState(m=m0, U=U0)
self.port_a = self.register_declared_port("port_a")
self.port_a = self.register_declared_port('port_a')
@classmethod
def create(
cls,
*,
name: str,
medium: IdealGasMedium,
parameters: Mapping[str, float],
) -> Tank:
return cls(
name=name,
medium=medium,
V=parameters["volume"],
p0=parameters["p0"],
T0=parameters["T0"],
)
def get_state_vector(self) -> list[float]:
return self.state.as_vector()
def set_state_vector(self, values: list[float]) -> None:
self.state = VolumeState.from_vector(values)
def properties(self) -> ThermodynamicProperties:
props = self.medium.properties_from_mU(self.state.m, self.state.U, self.V)
self.port_a.p = props.p
self.port_a.h_outflow = props.h
return props
def refresh_thermodynamic_ports(self) -> ThermodynamicProperties:
return self.properties()
def state_derivative_from_ports(
self,
connected_h: Mapping[str, float],
) -> list[float]:
properties = self.properties()
derivative = self.derivatives_from_connection(
connected_h=connected_h["port_a"],
port_m_flow=self.port_a.m_flow,
internal_h=properties.h,
)
return derivative.as_vector()
def pressure_flow_equation_residuals(self) -> tuple[EquationResidual, ...]:
pressure = self.medium.properties_from_mU(
self.state.m,
self.state.U,
self.V,
).p
return (
EquationResidual(
id=f"{self.name}:port_a_pressure_state",
owner="component",
owner_id=self.name,
relation="state",
variables=(f"{self.name}.port_a.p", f"{self.name}.state"),
role="effort",
value=self.port_a.p - pressure,
),
)
def derivatives_from_connection(
self,
*,
connected_h: float,
port_m_flow: float,
internal_h: float,
) -> VolumeState:
inlet_h = self.connection_inlet_enthalpy(
port_m_flow=port_m_flow,
connected_h=connected_h,
internal_h=internal_h,
)
return self.derivatives(inlet_h, port_m_flow)
def derivatives(self, inlet_h: float, m_flow: float) -> VolumeState:
return VolumeState(m=m_flow, U=m_flow * inlet_h)
def create(cls, *, name: str, medium: IdealGasMedium, parameters: Mapping[str, float]) -> Tank:
return cls(name=name, medium=medium, V=parameters['volume'], p0=parameters['p0'], T0=parameters['T0'])
EQUATIONS = ({'id': '__MODEL__:port_a_pressure_state', 'owner': 'component', 'ownerId': '__MODEL__', 'relation': 'state', 'variables': ['__MODEL__.port_a.p', '__MODEL__.state'], 'role': 'effort'},)