增加可选性能埋点并完成物性效率评估

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ljz committed 2026-08-16 17:46:04 +08:00
1 parent 4e0b9fd8cc
commit 57b459bc72
21 files changed
+2029 -179

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@@ -5,6 +5,8 @@ from app.simulation.core.errors import RecoverableTrialStateError
from dataclasses import dataclass
from math import acos, cos, isfinite, log, pi, sqrt
from app.simulation.performance import profile_property
UNIVERSAL_GAS_CONSTANT = 8.31446261815324
# Simcenter Amesim 2404 ``sag_reinit_eos_`` keeps more digits than the
# commonly printed Peng-Robinson constants 0.45724 and 0.07780.
@@ -97,6 +99,11 @@ class PengRobinsonFluid:
) -> float:
return self.a_parameter * self.alpha_temperature_second_derivative(temperature)
@profile_property(
"pressure_from_molar_volume",
layer="kernel",
minimum_mode="audit",
)
def pressure_from_molar_volume(self, temperature: float, molar_volume: float) -> float:
self._validate_temperature(temperature)
if molar_volume <= self.b_parameter:
@@ -107,11 +114,21 @@ class PengRobinsonFluid:
attractive = a_alpha / (molar_volume * (molar_volume + b) + b * (molar_volume - b))
return repulsive - attractive
@profile_property(
"pressure_from_density",
layer="kernel",
minimum_mode="audit",
)
def pressure_from_density(self, temperature: float, density: float) -> float:
if density <= 0.0:
raise ValueError("Density must be positive.")
return self.pressure_from_molar_volume(temperature, self.molar_mass / density)
@profile_property(
"pressure_temperature_derivative_at_density",
layer="kernel",
minimum_mode="audit",
)
def pressure_temperature_derivative_at_density(
self,
temperature: float,
@@ -132,6 +149,11 @@ class PengRobinsonFluid:
- self.attractive_parameter_temperature_derivative(temperature) / denominator
)
@profile_property(
"pressure_density_derivative_at_temperature",
layer="kernel",
minimum_mode="audit",
)
def pressure_density_derivative_at_temperature(
self,
temperature: float,
@@ -165,6 +187,11 @@ class PengRobinsonFluid:
B = b * pressure / (UNIVERSAL_GAS_CONSTANT * temperature)
return A, B
@profile_property(
"compressibility_roots",
layer="kernel",
minimum_mode="audit",
)
def compressibility_roots(self, pressure: float, temperature: float) -> tuple[float, ...]:
A, B = self.reduced_parameters(pressure, temperature)
coefficients = (
@@ -178,6 +205,11 @@ class PengRobinsonFluid:
raise ValueError("Peng-Robinson cubic produced no physical compressibility root.")
return physical_roots
@profile_property(
"compressibility_factor",
layer="kernel",
minimum_mode="audit",
)
def compressibility_factor(
self,
pressure: float,
@@ -193,6 +225,11 @@ class PengRobinsonFluid:
return roots[-1]
raise ValueError(f"Unsupported phase selector: {phase!r}")
@profile_property(
"molar_volume",
layer="kernel",
minimum_mode="audit",
)
def molar_volume(
self,
pressure: float,
@@ -202,6 +239,7 @@ class PengRobinsonFluid:
z = self.compressibility_factor(pressure, temperature, phase=phase)
return z * UNIVERSAL_GAS_CONSTANT * temperature / pressure
@profile_property("density", layer="kernel", minimum_mode="audit")
def density(
self,
pressure: float,
@@ -210,6 +248,11 @@ class PengRobinsonFluid:
) -> float:
return self.molar_mass / self.molar_volume(pressure, temperature, phase=phase)
@profile_property(
"residual_specific_enthalpy",
layer="kernel",
minimum_mode="audit",
)
def residual_specific_enthalpy(
self,
pressure: float,
@@ -239,6 +282,11 @@ class PengRobinsonFluid:
)
return residual_molar_enthalpy / self.molar_mass
@profile_property(
"residual_specific_internal_energy_at_density",
layer="kernel",
minimum_mode="audit",
)
def residual_specific_internal_energy_at_density(
self,
temperature: float,
@@ -268,6 +316,11 @@ class PengRobinsonFluid:
) * log(log_argument) / (2.0 * sqrt(2.0) * b)
return residual_molar_internal_energy / self.molar_mass
@profile_property(
"residual_isochoric_heat_capacity_at_density",
layer="kernel",
minimum_mode="audit",
)
def residual_isochoric_heat_capacity_at_density(
self,
temperature: float,