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SteamCalculator.py
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from library.iapws95 import IAPWS95
from STD_TYPES import *
from Phases import *
# the key is the key of property 1
# don't enter prop1 the same as prop2
# the second property must NOT be temperature or
# pressure as they are the same in saturated mixture you will not be able to calculate 'x'
def determine_key(typ):
"""Convert human-readable property names to internal representations."""
match typ:
case Temperature():
return "T"
case Pressure():
return "P"
case Enthalpy():
return "h"
case Entropy():
return "s"
case InternalEnergy():
return "u"
case Specific_Volume():
return "rho"
case X():
return "x"
return None
def determine_phase(prop_1, prop_2):
return determine_phase_helper(prop_1, prop_2, False)
def determine_phase_helper(prop_1, prop_2, flag):
prop_1_val = prop_1.data
prop_2_val = prop_2.data
key_prop_1 = determine_key(prop_1)
if isinstance(prop_1, X):
if prop_1_val > 1:
return Phases.SUPERHEATED, prop_1_val
elif prop_1_val < 0:
return Phases.SUBCOOLED, prop_1_val
elif 1 > prop_1_val > 0:
return Phases.SATMIXTURE, prop_1_val
elif prop_1_val == 0:
return Phases.SATLIQUID, prop_1_val
elif prop_1_val == 1:
return Phases.SATVAPOR, prop_1_val
if isinstance(prop_2, X):
if prop_2_val > 1:
return Phases.SUPERHEATED, prop_2_val
elif prop_2_val < 0:
return Phases.SUBCOOLED, prop_2_val
elif 1 > prop_2_val > 0:
return Phases.SATMIXTURE, prop_2_val
elif prop_2_val == 0:
return Phases.SATLIQUID, prop_2_val
elif prop_2_val == 1:
return Phases.SATVAPOR, prop_2_val
sat_liquid = None
sat_vapor = None
if key_prop_1 == "T":
prop_1_val += 273.15
elif key_prop_1 == "rho":
prop_1_val = 1 / prop_1_val
try:
param_1 = {key_prop_1: prop_1_val, "x": 0.0}
sat_liquid = IAPWS95(**param_1) # Saturated liquid
param_2 = {key_prop_1: prop_1_val, "x": 1.0}
sat_vapor = IAPWS95(**param_2) # Saturated vapor
p_f = None
p_g = None
x = None
match prop_2:
case Temperature():
if sat_liquid.T and sat_vapor.T:
p_f = sat_liquid.T - 273.15
p_g = sat_vapor.T - 273.15
else:
raise Exception("Retry with the other properties")
case Pressure():
if sat_liquid.P and sat_vapor.P:
p_f = sat_liquid.P
p_g = sat_vapor.P
else:
raise Exception("Retry with the other properties")
case Enthalpy():
if sat_liquid.h and sat_vapor.h:
p_f = sat_liquid.h
p_g = sat_vapor.h
else:
raise Exception("Retry with the other properties")
case Entropy():
if sat_liquid.s and sat_vapor.s:
p_f = sat_liquid.s
p_g = sat_vapor.s
else:
raise Exception("Retry with the other properties")
case Specific_Volume():
if sat_liquid.v and sat_vapor.v:
p_f = sat_liquid.v
p_g = sat_vapor.v
else:
raise Exception("Retry with the other properties")
case InternalEnergy():
if sat_liquid.u and sat_vapor.u:
p_f = sat_liquid.u
p_g = sat_vapor.u
else:
raise Exception("Retry with the other properties")
case _:
raise Exception("pass a valid property type")
except:
# to handle the case when the data is not sufficient to find sat. states from prop 1
# ,so we switch the order using this recursive call
# wrapping the function inside a helper function to prevent the stack overflow
if flag:
raise Exception("these properties cannot determine the phase !")
flag = True
return determine_phase_helper(prop_2, prop_1, flag)
if not p_f or not p_g: # this condition will not happen
raise Exception("p_f and p_g are not valid")
if (p_g - p_f) > 0:
x = (prop_2_val - p_f) / (p_g - p_f)
# Determine phase in case of pressure "the relation is inverse"
if isinstance(prop_2, Pressure):
if prop_2_val > p_f:
return Phases.SUBCOOLED, x
elif p_f <= prop_2_val <= p_g:
return Phases.SATMIXTURE, x
else:
return Phases.SUPERHEATED, x
else:
# Determine phase
if prop_2_val < p_f:
return Phases.SUBCOOLED, x
elif p_f <= prop_2_val <= p_g:
return Phases.SATMIXTURE, x
else:
return Phases.SUPERHEATED, x
class SteamCalculator:
def __init__(self):
self.properties = None
def pressure_with_temperature(self, pressure: Pressure, temperature: Temperature):
water = IAPWS95(P=pressure.data, T=temperature.data + 273.15)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def pressure_with_enthalpy(self, pressure: Pressure, enthalpy: Enthalpy):
water = IAPWS95(P=pressure.data, h=enthalpy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def pressure_with_entropy(self, pressure: Pressure, entropy: Entropy):
water = IAPWS95(P=pressure.data, s=entropy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def pressure_with_specific_volume(self, pressure: Pressure, s_volume: Specific_Volume): # ?
water = IAPWS95(P=pressure.data, rho=1 / s_volume.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def pressure_with_internal_energy(self, pressure: Pressure, internal_energy: InternalEnergy): # ?
try:
# phase, x = self.determine_phase_p_u(pressure.pressure, internal_energy.internal_energy)
phase, x = determine_phase(prop_1=pressure, prop_2=internal_energy)
except:
# I didn't pass as we need to find x to accurately determine U
return None
if phase == Phases.SATMIXTURE:
water = IAPWS95(P=pressure.data, x=x)
else:
water = IAPWS95(P=pressure.data, u=internal_energy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def temperature_with_enthalpy(self, temperature: Temperature, enthalpy: Enthalpy):
water = IAPWS95(T=temperature.data + 273.15, h=enthalpy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def temperature_with_entropy(self, temperature: Temperature, entropy: Entropy):
water = IAPWS95(T=temperature.data + 273.15, s=entropy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def temperature_with_specific_volume(self, temperature: Temperature, s_volume: Specific_Volume): # ?
water = IAPWS95(T=temperature.data + 273.15, rho=1 / s_volume.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def temperature_with_internal_energy(self, temperature: Temperature, internal_energy: InternalEnergy): # ?
water = IAPWS95(T=temperature.data + 273.15, u=internal_energy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def enthalpy_with_entropy(self, enthalpy: Enthalpy, entropy: Entropy):
water = IAPWS95(h=enthalpy.data, s=entropy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def enthalpy_with_specific_volume(self, enthalpy: Enthalpy, s_volume: Specific_Volume): # ?
water = IAPWS95(h=enthalpy.data, rho=1 / s_volume.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def enthalpy_with_internal_energy(self, enthalpy: Enthalpy, internal_energy: InternalEnergy): # ?
water = IAPWS95(h=enthalpy.data, u=internal_energy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def entropy_with_specific_volume(self, entropy: Entropy, s_volume: Specific_Volume): # ?
water = IAPWS95(s=entropy.data, rho=1 / s_volume.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def entropy_with_internal_energy(self, entropy: Entropy, internal_energy: InternalEnergy): # ?
water = IAPWS95(s=entropy.data, u=internal_energy.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def pressure_with_x(self, pressure: Pressure, x: X):
water = IAPWS95(P=pressure.data, x=x.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def temperature_with_x(self, temperature: Temperature, x: X):
water = IAPWS95(T=temperature.data + 273.15, x=x.data)
self.properties = self._get_properties(water)
if self.properties is not None:
return self.properties
def _get_properties(self, water: IAPWS95):
try:
self.properties = {
"Temperature (°C)": water.T - 273.15,
"Pressure (MPa)": water.P,
"Enthalpy (kJ/kg)": water.h,
"Entropy (kJ/kg·K)": water.s,
"Density (kg/m³)": water.rho,
"Internal Energy (kJ/kg)": water.u,
"Specific Volume (m³/kg)": 1 / water.rho,
"X": water.x
}
except:
return None
return self.properties
def display(self):
if self.properties is not None:
for key, val in self.properties.items():
print(f"{key}: {val}")