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CoolProp/dev/incompressible_liquids/CPIncomp/CoefficientFluids.py
2019-01-12 20:48:56 -07:00

42 lines
1.5 KiB
Python

from __future__ import division, print_function
import numpy as np
from .DataObjects import CoefficientData, PureData
class NitrateSalt(PureData, CoefficientData):
"""
Heat transfer fluid based on 60% NaNO3 and 40% KNO3
"""
def __init__(self):
CoefficientData.__init__(self)
PureData.__init__(self)
self.name = "NaK"
self.description = "Nitrate salt, 0.6 NaNO3 and 0.4 KNO3"
self.reference = "Zavoico2001"
self.Tmin = 300 + 273.15
self.Tmax = 600 + 273.15
self.TminPsat = self.Tmax
self.Tbase = 273.15
#self.temperature.data = self.getTrange()
# self.concentration.data = np.array([ 0 ]) # mass fraction
self.density.type = self.density.INCOMPRESSIBLE_POLYNOMIAL
self.density.source = self.density.SOURCE_COEFFS
self.density.coeffs = np.array([[2090], [-0.636]])
self.specific_heat.type = self.specific_heat.INCOMPRESSIBLE_POLYNOMIAL
self.specific_heat.source = self.specific_heat.SOURCE_COEFFS
self.specific_heat.coeffs = np.array([[1443], [+0.172]])
self.conductivity.type = self.conductivity.INCOMPRESSIBLE_POLYNOMIAL
self.conductivity.source = self.conductivity.SOURCE_COEFFS
self.conductivity.coeffs = np.array([[0.443], [+1.9e-4]])
self.viscosity.type = self.viscosity.INCOMPRESSIBLE_POLYNOMIAL
self.viscosity.source = self.viscosity.SOURCE_COEFFS
self.viscosity.coeffs = np.array([[22.714], [-0.120], [2.281 * 1e-4], [-1.474 * 1e-7]]) / 1e3