lujingze
e18399c022
同步远端 PNL0003 诊断和大采样网格能力，语义合并活动感知的 60 秒真停滞判定与旧后端 15 分钟兼容兜底。 纳管热路径优化、15 单元运行证据、浏览器与 API 报告，并补充北京时间更新日志和遗留问题。
122 lines
3.8 KiB
Python
122 lines
3.8 KiB
Python
from __future__ import annotations
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from collections.abc import Mapping
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from math import sqrt
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from app.simulation.core.base import AlgebraicComponent
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from app.simulation.core.catalog import ComponentDisplaySpec, PortDisplaySpec
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from app.simulation.core.equations import EquationResidual
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from app.simulation.core.metadata import ParameterDefinition
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from app.simulation.core.medium import IdealGasMedium
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from app.simulation.core.ports import PortDefinition
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class Orifice(AlgebraicComponent):
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"""Python port of ModelicaModels.Myorifice."""
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MODEL_TYPE = "orifice"
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MODEL_VERSION = "1.0.0"
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PRESSURE_FLOW_DEPENDS_ON_STREAM = False
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PRESSURE_FLOW_EXACT_SUM_TO_ZERO_EQUATION_SUFFIXES = frozenset(
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("mass_flow_balance",)
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)
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PORTS = (
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PortDefinition.pneumatic("port_a", nominal_role="inlet"),
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PortDefinition.pneumatic("port_b", nominal_role="outlet"),
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)
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PARAMETERS = (
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ParameterDefinition(
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"K",
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1e-5,
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label="流量系数",
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quantity="flow_coefficient",
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unit="kg/(s*Pa^0.5)",
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minimum=0.0,
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),
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ParameterDefinition(
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"opening",
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1.0,
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label="开度",
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minimum=0.0,
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maximum=1.0,
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),
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)
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RESULT_VARIABLES = ()
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DISPLAY = ComponentDisplaySpec(
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label="孔板/阀门",
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library_id="experimental",
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category_id="flow",
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symbol="orifice",
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ports=(
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PortDisplaySpec("port_a", "left", order=10),
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PortDisplaySpec("port_b", "right", order=20),
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),
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order=40,
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)
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def __init__(self, name: str, opening: float = 1.0, K: float = 1e-5) -> None:
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super().__init__(name=name)
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self.set_parameter_values({"K": K, "opening": opening})
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self.opening = opening
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self.K = K
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self.port_a = self.register_declared_port("port_a")
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self.port_b = self.register_declared_port("port_b")
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@classmethod
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def create(
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cls,
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*,
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name: str,
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medium: IdealGasMedium,
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parameters: Mapping[str, float],
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) -> Orifice:
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return cls(
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name=name,
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opening=parameters["opening"],
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K=parameters["K"],
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)
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@property
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def K_eff(self) -> float:
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return self.K * max(self.opening, 0.001)
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def mass_flow(self, p_a: float, p_b: float) -> float:
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dp = p_a - p_b
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if dp == 0.0:
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return 0.0
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return self.K_eff * sqrt(abs(dp)) * (1.0 if dp > 0.0 else -1.0)
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def pressure_flow_equation_residuals(self) -> tuple[EquationResidual, ...]:
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return (
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EquationResidual(
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id=f"{self.name}:mass_flow_balance",
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owner="component",
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owner_id=self.name,
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relation="sumToZero",
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variables=(
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f"{self.name}.port_a.m_flow",
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f"{self.name}.port_b.m_flow",
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),
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role="flow",
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value=self.port_a.m_flow + self.port_b.m_flow,
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),
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EquationResidual(
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id=f"{self.name}:pressure_flow_relation",
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owner="component",
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owner_id=self.name,
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relation="constitutive",
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variables=(
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f"{self.name}.port_a.p",
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f"{self.name}.port_b.p",
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f"{self.name}.port_a.m_flow",
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),
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role="flow",
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value=self.port_a.m_flow
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- self.mass_flow(self.port_a.p, self.port_b.p),
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),
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)
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def update_stream_outflows(self, connected_h: Mapping[str, float]) -> None:
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self.port_a.h_outflow = connected_h["port_b"]
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self.port_b.h_outflow = connected_h["port_a"]
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