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| Author | SHA1 | Date | |
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facb914417 | ||
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c5b85f5354 |
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+42
-18
@@ -11,15 +11,27 @@ from .components import (
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)
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from .cycles import BraytonCycle
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from .mass_models import (
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apply_component_mass,
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calculate_component_mass,
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condenser_radiator_mass,
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has_default_mass_model,
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heater_reactor_mass,
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initialize_recuperator_segments,
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recuperator_pche_mass,
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RecuperatorPCHEMassModel,
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turbine_tac_mass,
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PCHEGeometry,
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PCHEMaterial,
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PCHEDesignOptions,
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PCHE_STATE_UNIT_CONVENTION,
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calculate_condenser_mass,
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calculate_heater_mass,
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calculate_turbine_mass,
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calculate_water_outlet_temperature,
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flow_velocity,
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friction_factor,
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gnielinski_f_star,
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heat_transfer_coefficient,
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nusselt_number,
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overall_heat_transfer_coefficient,
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pche_channel_flow_area,
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pche_channel_wetted_perimeter,
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pche_equivalent_diameter,
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prandtl_number,
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pressure_drop_pa,
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reynolds_number,
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validate_pche_state,
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)
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from .optimization import (
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optimize_rc_fixed_param,
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@@ -44,24 +56,36 @@ __all__ = [
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"Concentrator",
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"Condenser",
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"Heater",
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"PCHEGeometry",
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"PCHEMaterial",
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"PCHEDesignOptions",
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"PCHE_STATE_UNIT_CONVENTION",
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"Recuperator",
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"RecuperatorPCHEMassModel",
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"Turbine",
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"apply_component_mass",
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"calculate_component_mass",
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"condenser_radiator_mass",
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"calculate_condenser_mass",
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"calculate_heater_mass",
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"calculate_turbine_mass",
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"calculate_water_outlet_temperature",
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"flow_velocity",
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"friction_factor",
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"gnielinski_f_star",
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"heat_transfer_coefficient",
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"evaluate_rc_efficiency",
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"has_default_mass_model",
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"heater_reactor_mass",
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"initialize_recuperator_segments",
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"local_rc_component_performance_sensitivity",
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"local_rc_design_sensitivity",
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"nusselt_number",
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"optimize_rc_fixed_param",
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"optimize_rc_param",
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"overall_heat_transfer_coefficient",
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"pche_channel_flow_area",
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"pche_channel_wetted_perimeter",
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"pche_equivalent_diameter",
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"plot_optimization_landscape",
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"plot_sweep_optimization_results",
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"recuperator_pche_mass",
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"prandtl_number",
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"pressure_drop_pa",
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"reynolds_number",
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"scan_rc_efficiency",
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"sweep_and_optimize_rc",
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"turbine_tac_mass",
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"validate_pche_state",
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]
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+90
-18
@@ -1,9 +1,15 @@
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# -*- coding: utf-8 -*-
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"""Component models used by Brayton cycle simulations."""
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from .mass_models import (
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calculate_condenser_mass,
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calculate_heater_mass,
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calculate_turbine_mass,
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)
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class ComponentMassMixin:
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"""Shared mass-result storage interface for cycle components."""
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"""Shared mass-calculation interface for cycle components."""
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component_type = "component"
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@@ -11,16 +17,43 @@ class ComponentMassMixin:
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self.mass = None
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self.mass_variables = None
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def set_mass_result(self, result):
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"""Store a mass-model result on this component.
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def calculate_mass(self, mass_model=None, **kwargs):
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"""Calculate and store component mass.
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Mass formulas live in ``brayton_cycle.mass_models``. Components only
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keep the result after their thermodynamic calculator has populated
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``variables``.
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The future mass model can be provided as either a callable accepting
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``(component, **kwargs)`` or an object exposing ``calculate_mass`` or
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``calculate_<component_type>_mass``.
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"""
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if self.variables is None:
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raise ValueError("Run component calculator before storing mass")
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raise ValueError("Run component calculator before mass calculation")
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if mass_model is None:
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result = self._calculate_mass(**kwargs)
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else:
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result = self._run_external_mass_model(mass_model, **kwargs)
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return self._store_mass_result(result)
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def mass_calculator(self, mass_model=None, **kwargs):
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return self.calculate_mass(mass_model=mass_model, **kwargs)
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def _calculate_mass(self, **kwargs):
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raise NotImplementedError(
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f"{self.__class__.__name__} mass model is not implemented yet. "
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"Pass a mass_model or override _calculate_mass()."
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)
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def _run_external_mass_model(self, mass_model, **kwargs):
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method_name = f"calculate_{self.component_type}_mass"
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if hasattr(mass_model, method_name):
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return getattr(mass_model, method_name)(self, **kwargs)
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if hasattr(mass_model, "calculate_mass"):
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return mass_model.calculate_mass(self, **kwargs)
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if callable(mass_model):
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return mass_model(self, **kwargs)
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raise TypeError("mass_model must be callable or expose a supported method")
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def _store_mass_result(self, result):
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if isinstance(result, dict):
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if "mass" in result:
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mass = result["mass"]
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@@ -39,17 +72,8 @@ class ComponentMassMixin:
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self.variables["mass_variables"] = self.mass_variables
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return self.mass
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def clear_mass_result(self):
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self.mass = None
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self.mass_variables = None
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if self.variables is not None:
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self.variables.pop("mass", None)
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self.variables.pop("mass_variables", None)
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class Compressor(ComponentMassMixin):
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class Compressor():
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"""压缩机类"""
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component_type = "compressor"
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def __init__(self, name, eff):
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"""
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初始化参数
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@@ -65,7 +89,6 @@ class Compressor(ComponentMassMixin):
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self.name = name
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self.eff = eff
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self.variables = None
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self._init_mass_interface()
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def calculator(self, p_in, T_in, p_out, property_calculator):
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# 先计算熵值
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@@ -144,6 +167,9 @@ class Turbine(ComponentMassMixin):
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'pi': p_in / p_out
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}
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def _calculate_mass(self, Pe=None, A=0.5, **kwargs):
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return calculate_turbine_mass(self, Pe=Pe, A=A, **kwargs)
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class Recuperator(ComponentMassMixin):
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"""换热器类"""
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component_type = "recuperator"
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@@ -334,6 +360,23 @@ class Heater(ComponentMassMixin):
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'Q_in': Q_input,
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}
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def _calculate_mass(
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self,
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P_heat_mwt=None,
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mass_flow_rate=None,
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shielding_mass_ton=2.8,
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include_shielding=True,
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**kwargs,
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):
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return calculate_heater_mass(
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self,
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P_heat_mwt=P_heat_mwt,
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mass_flow_rate=mass_flow_rate,
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shielding_mass_ton=shielding_mass_ton,
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include_shielding=include_shielding,
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**kwargs,
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)
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class Condenser(ComponentMassMixin):
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"""冷凝器类"""
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component_type = "condenser"
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@@ -362,6 +405,35 @@ class Condenser(ComponentMassMixin):
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'Q_out': Q_output,
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}
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def _calculate_mass(
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self,
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Qc_kw=None,
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co2_mass_flow_rate=None,
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coolant_outlet_T=None,
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water_inlet_T=None,
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water_mass_flow_rate=None,
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water_pressure_kpa=101.325,
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refprop_path="C:/Program Files (x86)/REFPROP 10.0+/REFPROP",
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emissivity=0.92,
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surface_temperature=210.15,
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area_density=6.75,
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**kwargs,
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):
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return calculate_condenser_mass(
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self,
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Qc_kw=Qc_kw,
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co2_mass_flow_rate=co2_mass_flow_rate,
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coolant_outlet_T=coolant_outlet_T,
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water_inlet_T=water_inlet_T,
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water_mass_flow_rate=water_mass_flow_rate,
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water_pressure_kpa=water_pressure_kpa,
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refprop_path=refprop_path,
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emissivity=emissivity,
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surface_temperature=surface_temperature,
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area_density=area_density,
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**kwargs,
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)
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class Concentrator(ComponentMassMixin):
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"""汇流组件"""
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component_type = "concentrator"
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+6
-30
@@ -9,7 +9,6 @@ from .components import (
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Recuperator,
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Turbine,
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)
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from .mass_models import apply_component_mass, has_default_mass_model
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from .properties import CO2PropertyCalculator
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@@ -58,31 +57,13 @@ class BraytonCycle:
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else:
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yield value
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def calculate_component_masses(self, mass_model=None, strict=False, **kwargs):
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def calculate_component_masses(self, mass_model=None, **kwargs):
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"""Calculate mass for each initialized component."""
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component_masses = {}
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for component in self.iter_components():
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if not hasattr(component, "set_mass_result"):
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if not hasattr(component, "calculate_mass"):
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continue
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if mass_model is None and not has_default_mass_model(component):
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if strict:
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raise NotImplementedError(
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f"No default mass model for component type "
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f"{component.component_type!r}."
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)
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continue
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try:
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mass = apply_component_mass(
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component,
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mass_model=mass_model,
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**kwargs,
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)
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except NotImplementedError:
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if strict:
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raise
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continue
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mass = component.calculate_mass(mass_model=mass_model, **kwargs)
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key = component.variables.get("name", component.name)
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component_masses[key] = {
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"component_type": component.component_type,
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@@ -93,23 +74,18 @@ class BraytonCycle:
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self.component_masses = component_masses
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return self.component_masses
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def cycle_mass_calculator(self, mass_model=None, strict=False, **kwargs):
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def cycle_mass_calculator(self, mass_model=None, **kwargs):
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"""Calculate and return total cycle component mass."""
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component_masses = self.calculate_component_masses(
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mass_model=mass_model,
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strict=strict,
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**kwargs,
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)
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self.total_mass = sum(item["mass"] for item in component_masses.values())
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return self.total_mass
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def calculate_total_mass(self, mass_model=None, strict=False, **kwargs):
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def calculate_total_mass(self, mass_model=None, **kwargs):
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"""Compatibility alias for cycle_mass_calculator."""
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return self.cycle_mass_calculator(
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mass_model=mass_model,
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strict=strict,
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**kwargs,
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)
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return self.cycle_mass_calculator(mass_model=mass_model, **kwargs)
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def SC(self, T_low, T_high, p_low, p_high, param=None):
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"""Simple Brayton cycle."""
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+309
-686
File diff suppressed because it is too large.
Load diff
+28
-11
@@ -15,7 +15,7 @@ class CO2PropertyCalculator():
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self.rp.SETUPdll(2, 'SI', 'SI', 'DEF')
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self.z = [1.0]
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self.mw = self.rp.WMOLdll(self.z)
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def calculate_properties(self, T=None, P=None, h=None, s=None):
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def calculate_properties(self, T=None, P=None, h=None, s=None, include_transport=False):
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"""计算二氧化碳物性"""
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if T is not None and P is not None:
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# 已知Tp
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@@ -60,15 +60,32 @@ class CO2PropertyCalculator():
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# 补充提取的物性,这里由于后续还要使用,不进行参数变换
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properties['D'] = result.D
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properties['density_kg_m3'] = result.D * self.mw
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properties['cp'] = result.Cp
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properties['cp_j_kg_k'] = result.Cp / self.mw * 1000
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properties['cv'] = result.Cv
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properties['cv_j_kg_k'] = result.Cv / self.mw * 1000
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transport = self.rp.TRNPRPdll(result.T, result.D, self.z)
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if transport.ierr > 0:
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raise ValueError(f"REFPROP transport calculation error:{transport.ierr}")
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properties['viscosity_pa_s'] = transport.eta * 1e-6
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properties['thermal_conductivity_w_m_k'] = transport.tcx
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properties['cv'] = result.Cv,
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properties['rho'] = result.D * self.mw
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properties['cp_mass'] = result.Cp / self.mw * 1000.0
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properties['cv_mass'] = result.Cv / self.mw * 1000.0
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if include_transport:
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self._add_transport_properties(properties, result)
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return properties
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def _add_transport_properties(self, properties, result):
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"""Add CO2 transport properties needed by PCHE correlations."""
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transport = self.rp.TRNPRPdll(properties['T'], result.D, self.z)
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if getattr(transport, 'ierr', 0) > 0:
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raise ValueError(f"REFPROP transport calculation error:{transport.ierr}")
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viscosity_micro_pa_s = getattr(transport, 'eta', None)
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thermal_conductivity = getattr(transport, 'tcx', None)
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if viscosity_micro_pa_s is None:
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viscosity_micro_pa_s = getattr(transport, 'visc', None)
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if thermal_conductivity is None:
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thermal_conductivity = getattr(transport, 'tcond', None)
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if viscosity_micro_pa_s is None or thermal_conductivity is None:
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raise ValueError("REFPROP transport result missing viscosity or conductivity")
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viscosity_pa_s = viscosity_micro_pa_s * 1.0e-6
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properties['mu'] = viscosity_pa_s
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properties['viscosity'] = viscosity_pa_s
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properties['lambda'] = thermal_conductivity
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properties['thermal_conductivity'] = thermal_conductivity
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Reference in new issue
Block a user