SystemSimulationApp/app/simulation/components/experimental/flow/resistive_pipe.py

from __future__ import annotations

from collections.abc import Mapping
from math import pi

from app.simulation.core.base import AlgebraicComponent
from app.simulation.core.catalog import ComponentDisplaySpec, PortDisplaySpec
from app.simulation.core.equations import EquationResidual
from app.simulation.core.metadata import ParameterDefinition
from app.simulation.core.medium import IdealGasMedium
from app.simulation.core.ports import PortDefinition


class ResistivePipe(AlgebraicComponent):
    """Quasi-steady Darcy resistance used by topology-driven simulation."""

    MODEL_TYPE = "pipe"
    MODEL_VERSION = "1.0.0"
    PRESSURE_FLOW_DEPENDS_ON_STREAM = False
    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 = ()
    DISPLAY = ComponentDisplaySpec(
        label="管段",
        library_id="experimental",
        category_id="flow",
        symbol="pipe",
        ports=(
            PortDisplaySpec("port_a", "left", order=10),
            PortDisplaySpec("port_b", "right", order=20),
        ),
        order=30,
    )

    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

    @classmethod
    def create(
        cls,
        *,
        name: str,
        medium: IdealGasMedium,
        parameters: Mapping[str, float],
    ) -> ResistivePipe:
        return cls(
            name=name,
            medium=medium,
            L=parameters["length"],
            D=parameters["diameter"],
            lambda_darcy=parameters["lambda_darcy"],
            p0=parameters["p0"],
            T0=parameters["T0"],
        )

    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"]