对齐PNL0002上游温度并稳定热流体闭合

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huojiarong committed 2026-08-11 07:12:52 +00:00
1 parent 6abcc220de
commit 0f73d5b568
5 files changed
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@@ -40,6 +40,10 @@ class SimulationPreparationError(ValueError):
self.issues = issues
class ThermofluidClosureError(RuntimeError):
"""Raised when stream enthalpy and pressure-flow do not reach one fixed point."""
@dataclass(frozen=True)
class GenericSimulationResult:
success: bool
@@ -260,6 +264,7 @@ class GenericFluidSystem:
self.max_algebraic_residual = 0.0
self.max_algebraic_evaluations = 0
self.max_stream_iterations = 0
self.max_thermofluid_iterations = 0
self.signal_propagation_count = 0
self.pneumatic_volume_propagation_count = 0
@@ -280,20 +285,62 @@ class GenericFluidSystem:
for component in self.dynamic_components:
component.refresh_thermodynamic_ports()
algebraic = self.pressure_flow_solver.solve()
pressure_flow_solve_count = 1
pneumatic_volume = self.pneumatic_volume_resolver.solve()
self.pneumatic_volume_propagation_count += pneumatic_volume.propagated
if pneumatic_volume.propagated:
for component in self.dynamic_components:
component.refresh_thermodynamic_ports()
algebraic = self.pressure_flow_solver.solve()
stream, connected_h = self.stream_resolver.solve()
pressure_flow_solve_count += 1
# Some constitutive flow laws recover their upstream temperature from
# the connected stream enthalpy. Stream propagation updates that
# cache after the first pressure-flow pass, so refresh explicit flows
# once more before evaluating state derivatives and result variables.
algebraic = self.pressure_flow_solver.solve()
# connected stream enthalpy, while junction stream mixing itself depends
# on the resulting mass flows. A single stream -> pressure-flow refresh
# leaves that two-way coupling to the next RHS call, making the ODE RHS
# depend on evaluation history and corrupting finite-difference
# Jacobians. Close both layers to one fixed point inside this call.
physical_ports = tuple(
port
for component in self.network.components.values()
for definition in component.port_definitions
if definition.kind == "physical"
for port in (component.get_port(definition.name),)
)
connected_h: dict[str, dict[str, float]] = {}
max_coupling_iterations = 25
flow_relative_tolerance = 1.0e-12
for coupling_iteration in range(1, max_coupling_iterations + 1):
previous_flows = tuple(port.m_flow for port in physical_ports)
stream, connected_h = self.stream_resolver.solve()
for component in self.dynamic_components:
component.update_stream_outflows(connected_h[component.name])
algebraic = self.pressure_flow_solver.solve()
pressure_flow_solve_count += 1
current_flows = tuple(port.m_flow for port in physical_ports)
flow_scale = max(
[abs(value) for value in (*previous_flows, *current_flows)] + [1.0]
)
max_flow_delta = max(
(
abs(current - previous)
for previous, current in zip(previous_flows, current_flows)
),
default=0.0,
)
if max_flow_delta <= flow_relative_tolerance * flow_scale:
break
else:
raise ThermofluidClosureError(
"Stream enthalpy and pressure-flow coupling did not converge "
f"after {max_coupling_iterations} iterations."
)
self.max_thermofluid_iterations = max(
self.max_thermofluid_iterations,
coupling_iteration,
)
self.mechanical_state_reducer.update_constraint_accelerations()
self.algebraic_solve_count += 2 + int(bool(pneumatic_volume.propagated))
self.algebraic_solve_count += pressure_flow_solve_count
self.max_algebraic_residual = max(
self.max_algebraic_residual,
algebraic.max_scaled_residual,
@@ -467,6 +514,7 @@ class GenericFluidSystem:
},
"stream": {
"maxIterationsPerSolve": self.max_stream_iterations,
"maxThermofluidIterations": self.max_thermofluid_iterations,
"last": (
self.stream_resolver.last_diagnostics.as_dict()
if self.stream_resolver.last_diagnostics is not None