修正动态管与阀门诊断输出

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huojiarong committed 2026-08-18 10:24:29 +00:00
1 parent f725f038b6
commit 53f8601fec
6 files changed
+219 -16

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@@ -35,6 +35,7 @@ _FLOWSET_USES_CV = (ParameterCondition("flowset", (2.0,)),)
_FLOWSET_USES_KV = (ParameterCondition("flowset", (3.0,)),)
_PN_PRESSURE_RATIO_ACCURACY = 0.9999
_PN_LAMINAR_SMOOTHING_GAIN = 12.0
_PNVO001_CLOSED_OPENING_ABS_TOL = 1.0e-12
_PNOR001_FLOW_COEFFICIENT_GROUP = ParameterGroupDisplaySpec(
id="flow_coefficient",
label="流量系数",
@@ -835,6 +836,16 @@ class AmesimPnvo001FixedOpening(AlgebraicComponent):
downstream_pressure=downstream_pressure,
upstream_temperature=upstream_temperature,
)
# AMESim reports no vena-contracta velocity while the valve is closed.
# Signal propagation around a step can leave a round-off-sized opening,
# so apply the same numerical-zero convention to this diagnostic only.
if isclose(
self.opening,
0.0,
rel_tol=0.0,
abs_tol=_PNVO001_CLOSED_OPENING_ABS_TOL,
):
gas_velocity = 0.0
return {
"xv": self.opening,
"cm": mass_flow_parameter,
+55 -15
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@@ -75,6 +75,31 @@ def _reported_friction_factor(value: float) -> float:
return min(float(value), _MAX_REPORTED_FRICTION_FACTOR)
def _bare_pipe_mass_flow_parameter(
mass_flow: float,
*,
area: float,
diameter: float,
upstream_pressure: float,
upstream_temperature: float,
resistance_length: float,
friction_factor: float,
) -> float:
"""Return Amesim's ``Cm`` without the pipe flow coefficient ``Cq``."""
flow_coefficient = sqrt(
diameter / (resistance_length * friction_factor)
)
return (
abs(mass_flow)
* sqrt(upstream_temperature)
/ max(
flow_coefficient * area * upstream_pressure,
1.0e-18,
)
)
_DYNAMIC_PIPE_POLYTROPIC_MODE = ParameterCondition("mode", (1.0,))
_DYNAMIC_PIPE_HEAT_EXCHANGE_MODE = ParameterCondition("mode", (2.0,))
_DYNAMIC_PIPE_PARAMETER_GROUPS = (
@@ -1014,6 +1039,7 @@ class AmesimPnl0001(ThermodynamicVolumeComponent):
upstream_pressure = max(self.port_1.p, props.p, 1.0)
density = max(self.medium.density(upstream_pressure, props.T), 1.0e-12)
reynolds = self.reynolds_number(flow, props.T)
friction = self.friction_factor(reynolds)
return {
"m": self.state.m,
"U": self.state.U,
@@ -1023,13 +1049,17 @@ class AmesimPnl0001(ThermodynamicVolumeComponent):
"u": props.u,
"h": props.h,
"re": reynolds,
"cm": (
abs(flow)
* sqrt(props.T)
/ max(self.area * upstream_pressure, 1.0e-18)
"cm": _bare_pipe_mass_flow_parameter(
flow,
area=self.area,
diameter=self.diam,
upstream_pressure=upstream_pressure,
upstream_temperature=props.T,
resistance_length=self.le,
friction_factor=friction,
),
"v": flow / (density * self.area),
"ff": _reported_friction_factor(self.friction_factor(reynolds)),
"ff": _reported_friction_factor(friction),
}
def pressure_flow_equation_values(self) -> tuple[float, ...]:
@@ -1344,16 +1374,21 @@ class AmesimPnl0002(AmesimPnl0001):
1.0e-12,
)
reynolds = self.reynolds_number(flow, upstream_temperature)
friction = self.friction_factor(reynolds)
resistance_diagnostics.append(
(
reynolds,
(
abs(flow)
* sqrt(upstream_temperature)
/ max(self.area * upstream_pressure, 1.0e-18)
_bare_pipe_mass_flow_parameter(
flow,
area=self.area,
diameter=self.diam,
upstream_pressure=upstream_pressure,
upstream_temperature=upstream_temperature,
resistance_length=self.resistance_length,
friction_factor=friction,
),
abs(flow) / (density * self.area),
self.friction_factor(reynolds),
friction,
)
)
reynolds, cm, velocity, friction = (
@@ -1699,6 +1734,7 @@ class AmesimPnl0003(DynamicComponent):
center_flow = self.resistance_mass_flow()
upstream = port_1 if center_flow >= 0.0 else port_2
reynolds = self.reynolds_number(center_flow, upstream.T)
friction = self.friction_factor(reynolds)
return {
"m1": self.state_1.m,
"U1": self.state_1.U,
@@ -1716,13 +1752,17 @@ class AmesimPnl0003(DynamicComponent):
"h2": port_2.h,
"dmctr": center_flow,
"re": reynolds,
"cm": (
abs(center_flow)
* sqrt(upstream.T)
/ max(self.area * max(port_1.p, port_2.p, 1.0), 1.0e-18)
"cm": _bare_pipe_mass_flow_parameter(
center_flow,
area=self.area,
diameter=self.diam,
upstream_pressure=max(port_1.p, port_2.p, 1.0),
upstream_temperature=upstream.T,
resistance_length=self.le,
friction_factor=friction,
),
"v": center_flow / (max(upstream.rho, 1.0e-12) * self.area),
"ff": _reported_friction_factor(self.friction_factor(reynolds)),
"ff": _reported_friction_factor(friction),
}
def pressure_flow_equation_values(self) -> tuple[float, ...]:
+28
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@@ -1,6 +1,7 @@
from __future__ import annotations
import unittest
from math import sqrt
from app.simulation.components.amesim.flow.pipes import AmesimPnl0001
from app.simulation.core.medium import IdealGasMedium
@@ -148,6 +149,33 @@ class AmesimPnl0001ComponentTests(unittest.TestCase):
{"m", "U", "p", "T", "rho", "u", "h", "re", "cm", "v", "ff"},
)
def test_result_cm_excludes_pipe_flow_coefficient(self) -> None:
pipe = AmesimPnl0001(
"pnl_1",
self.medium,
diam=0.014,
le=0.3,
rr=0.045 / 14.0,
p0=2.5e6,
T0=290.0,
)
pipe.port_1.p = 1.6e6
props = pipe.properties()
flow = pipe.mass_flow(pipe.port_1.p, props.p, props.T)
reynolds = pipe.reynolds_number(flow, props.T)
friction = pipe.friction_factor(reynolds)
raw_cq_cm = (
abs(flow)
* sqrt(props.T)
/ (pipe.area * max(pipe.port_1.p, props.p))
)
flow_coefficient = sqrt(pipe.diam / (pipe.le * friction))
actual = pipe.component_result_values()["cm"]
self.assertAlmostEqual(actual, raw_cq_cm / flow_coefficient)
self.assertNotAlmostEqual(actual, raw_cq_cm)
if __name__ == "__main__":
unittest.main()
+104 -1
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@@ -1,7 +1,7 @@
from __future__ import annotations
import unittest
from math import log10
from math import log10, sqrt
from app.simulation.components.amesim.flow.pipes import AmesimPnl0002, AmesimPnl0003
from app.simulation.core.medium import IdealGasMedium
@@ -200,6 +200,79 @@ class AmesimPnl0002ComponentTests(unittest.TestCase):
self.assertAlmostEqual(derivative[0], 0.3)
self.assertAlmostEqual(derivative[1], 0.3 * props.h)
def test_result_cm_averages_bare_parameter_for_each_resistance(self) -> None:
pipe = AmesimPnl0002(
"pnl_2",
self.medium,
diam=0.02,
le=2.0,
rr=0.045 / 20.0,
p0=100000.0,
T0=350.0,
)
center = pipe.properties()
pipe.port_1.p = 130000.0
pipe.port_2.p = 80000.0
pipe.update_flow_temperature_references(
{
"port_1": self.medium.specific_enthalpy_at_pressure(
pipe.port_1.p,
250.0,
),
"port_2": self.medium.specific_enthalpy_at_pressure(
pipe.port_2.p,
450.0,
),
}
)
raw_parameters: list[float] = []
bare_parameters: list[float] = []
frictions: list[float] = []
for port_name, port in (
("port_1", pipe.port_1),
("port_2", pipe.port_2),
):
flow = pipe.port_mass_flow(
port.p,
center.p,
center.T,
port_name=port_name,
)
if flow >= 0.0:
upstream_pressure = port.p
upstream_temperature = pipe.medium.temperature_from_pressure_enthalpy(
port.p,
pipe._connected_h[port_name],
)
else:
upstream_pressure = center.p
upstream_temperature = center.T
reynolds = pipe.reynolds_number(flow, upstream_temperature)
friction = pipe.friction_factor(reynolds)
raw = (
abs(flow)
* sqrt(upstream_temperature)
/ (pipe.area * upstream_pressure)
)
flow_coefficient = sqrt(
pipe.diam / (pipe.resistance_length * friction)
)
raw_parameters.append(raw)
bare_parameters.append(raw / flow_coefficient)
frictions.append(friction)
expected = sum(bare_parameters) / 2.0
collapsed = (sum(raw_parameters) / 2.0) / sqrt(
pipe.diam
/ (pipe.resistance_length * (sum(frictions) / 2.0))
)
actual = pipe.component_result_values()["cm"]
self.assertAlmostEqual(actual, expected)
self.assertGreater(abs(actual - collapsed), 1.0e-8)
class AmesimPnl0003ComponentTests(unittest.TestCase):
def setUp(self) -> None:
@@ -389,6 +462,36 @@ class AmesimPnl0003ComponentTests(unittest.TestCase):
self.assertIn("dmctr", values)
self.assertIn("re", values)
def test_result_cm_excludes_center_resistance_flow_coefficient(self) -> None:
pipe = AmesimPnl0003(
"pnl_3",
self.medium,
diam=0.02,
le=0.3,
rr=0.045 / 20.0,
p1_0=10.7e6,
T1_0=263.4,
p2_0=10.68e6,
T2_0=263.42,
)
port_1 = pipe.properties_1()
port_2 = pipe.properties_2()
flow = pipe.resistance_mass_flow()
upstream = port_1 if flow >= 0.0 else port_2
reynolds = pipe.reynolds_number(flow, upstream.T)
friction = pipe.friction_factor(reynolds)
raw_cq_cm = (
abs(flow)
* sqrt(upstream.T)
/ (pipe.area * max(port_1.p, port_2.p))
)
flow_coefficient = sqrt(pipe.diam / (pipe.le * friction))
actual = pipe.component_result_values()["cm"]
self.assertAlmostEqual(actual, raw_cq_cm / flow_coefficient)
self.assertNotAlmostEqual(actual, raw_cq_cm)
if __name__ == "__main__":
unittest.main()
@@ -54,6 +54,25 @@ class AmesimPnvo001FixedOpeningComponentTests(unittest.TestCase):
self.assertEqual(valve.mass_flow(500000.0, 100000.0), 0.0)
def test_closed_opening_only_zeroes_reported_gas_velocity(self) -> None:
valve = AmesimPnvo001FixedOpening("valve_1", self.medium, opening=0.0)
valve.port_2.p = 500000.0
valve.port_3.p = 100000.0
closed = valve.component_result_values()
self.assertGreater(closed["cm"], 0.0)
self.assertEqual(closed["gasvel"], 0.0)
valve.opening = 7.0e-15
roundoff_closed = valve.component_result_values()
self.assertEqual(roundoff_closed["gasvel"], 0.0)
self.assertEqual(roundoff_closed["cm"], closed["cm"])
valve.opening = 1.0e-9
genuinely_open = valve.component_result_values()
self.assertNotEqual(genuinely_open["gasvel"], 0.0)
self.assertEqual(genuinely_open["cm"], closed["cm"])
def test_mass_flow_is_bidirectional_by_pressure_order(self) -> None:
valve = AmesimPnvo001FixedOpening("valve_1", self.medium, opening=0.5)
+2
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@@ -244,6 +244,8 @@ class AmesimPnvo001SignalXmlTests(unittest.TestCase):
self.assertEqual(result["series"]["step_1.out.signal"][at_event], 1.0)
self.assertEqual(result["series"]["valve_1.xv"][before_event], 0.0)
self.assertEqual(result["series"]["valve_1.xv"][at_event], 1.0)
self.assertEqual(result["series"]["valve_1.gasvel"][before_event], 0.0)
self.assertNotEqual(result["series"]["valve_1.gasvel"][at_event], 0.0)
self.assertGreater(
result["series"]["valve_1.port_2.m_flow"][at_event],
0.45,