Add IAPWS water density data

This commit is contained in:
Sterling Harper 2018-02-10 01:04:45 -05:00
parent 1b095929a0
commit bb4ac5a7b2
2 changed files with 117 additions and 0 deletions

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@ -1,6 +1,9 @@
import itertools
import os
import re
from warnings import warn
from numpy import sqrt
# Isotopic abundances from Meija J, Coplen T B, et al, "Isotopic compositions
@ -208,6 +211,110 @@ def atomic_weight(element):
return None if weight == 0. else weight
def water_density(temperature, pressure=0.1013):
"""Return the density of liquid water at a given temperature and pressure.
The density is calculated from a polynomial fit using equations and values
from the 2012 version of the IAPWS-IF97 formulation. Only the equations
for region 1 are implemented here.
Results are invalid for water vapor; pressures above 100 [MPa]; and
temperatures below 273.15 [K], above 623.15 [K], or above saturation.
Reference: International Association for the Properties of Water and Steam,
"Revised Release on the IAPWS Industrial Formulation 1997 for the
Thermodynamic Properties of Water and Steam", IAPWS R7-97(2012).
Parameters
----------
temperature : float
Water temperature in units of [K]
pressure : float
Water pressure in units of [MPa]
Returns
-------
float
Water density in units of [g / cm^3]
"""
# Make sure the temperature and pressure are inside the min/max region 1
# bounds. (Relax the 273.15 bound to 273 in case a user wants 0 deg C data
# but they only use 3 digits for their conversion to K.)
if pressure > 100.0:
warn("Results are not valid for pressures above 100 MPa.")
if pressure < 0.0:
warn("Results are not valid for pressures below zero.")
if temperature < 273:
warn("Results are not valid for temperatures below 273.15 K.")
if temperature > 623.15:
warn("Results are not valid for temperatures above 623.15 K.")
# IAPWS region 4 parameters
_n4 = [0.11670521452767e4, -0.72421316703206e6, -0.17073846940092e2,
0.12020824702470e5, -0.32325550322333e7, 0.14915108613530e2,
-0.48232657361591e4, 0.40511340542057e6, -0.23855557567849,
0.65017534844798e3]
# Compute the saturation temperature at the given pressure.
beta = pressure**(0.25)
E = beta**2 + _n4[2] * beta + _n4[5]
F = _n4[0] * beta**2 + _n4[3] * beta + _n4[6]
G = _n4[1] * beta**2 + _n4[4] * beta + _n4[7]
D = 2.0 * G / (-F - sqrt(F**2 - 4 * E * G))
T_sat = 0.5 * (_n4[9] + D
- sqrt((_n4[9] + D)**2 - 4.0 * (_n4[8] + _n4[9] * D)))
# Make sure we aren't above saturation. (Relax this bound by .2 degrees
# for deg C to K conversions.)
if temperature > T_sat + 0.2:
warn("Results are not valid for temperatures above saturation "
"(above the boiling point).")
# IAPWS region 1 parameters
R_GAS_CONSTANT = 0.461526 # kJ / kg / K
_ref_p = 16.53 # MPa
_ref_T = 1386 # K
_n1f = [0.14632971213167, -0.84548187169114, -0.37563603672040e1,
0.33855169168385e1, -0.95791963387872, 0.15772038513228,
-0.16616417199501e-1, 0.81214629983568e-3, 0.28319080123804e-3,
-0.60706301565874e-3, -0.18990068218419e-1, -0.32529748770505e-1,
-0.21841717175414e-1, -0.52838357969930e-4, -0.47184321073267e-3,
-0.30001780793026e-3, 0.47661393906987e-4, -0.44141845330846e-5,
-0.72694996297594e-15, -0.31679644845054e-4, -0.28270797985312e-5,
-0.85205128120103e-9, -0.22425281908000e-5, -0.65171222895601e-6,
-0.14341729937924e-12, -0.40516996860117e-6, -0.12734301741641e-8,
-0.17424871230634e-9, -0.68762131295531e-18, 0.14478307828521e-19,
0.26335781662795e-22, -0.11947622640071e-22, 0.18228094581404e-23,
-0.93537087292458e-25]
_I1f = [0, 0, 0, 0, 0, 0, 0, 0, 1, 1, 1, 1, 1, 1, 2, 2, 2, 2, 2, 3, 3, 3, 4,
4, 4, 5, 8, 8, 21, 23, 29, 30, 31, 32]
_J1f = [-2, -1, 0, 1, 2, 3, 4, 5, -9, -7, -1, 0, 1, 3, -3, 0, 1, 3, 17, -4,
0, 6, -5, -2, 10, -8, -11, -6, -29, -31, -38, -39, -40, -41]
# Nondimensionalize the pressure and temperature.
pi = pressure / _ref_p
tau = _ref_T / temperature
# Compute the derivative of gamma (dimensionless Gibbs free energy) with
# respect to pi.
gamma1_pi = 0.0
for i in range(34):
gamma1_pi -= (_n1f[i] * _I1f[i] * (7.1 - pi)**(_I1f[i] - 1)
* (tau - 1.222)**_J1f[i])
# Compute the leading coefficient. This sets the units at
# 1 [MPa] * [kg K / kJ] / [1 / K]
# = 1e6 [N / m^2] * 1e-3 [kg K / N / m] * [1 / K]
# = 1e3 [kg / m^3]
# = 1 [g / cm^3]
coeff = pressure / R_GAS_CONSTANT / temperature
# Compute and return the density.
return coeff / pi / gamma1_pi
# Values here are from the Committee on Data for Science and Technology
# (CODATA) 2014 recommendation (doi:10.1103/RevModPhys.88.035009).

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@ -48,3 +48,13 @@ def test_thin():
x_thin, y_thin = openmc.data.thin(x, y)
f = openmc.data.Tabulated1D(x_thin, y_thin)
assert f(1.0) == pytest.approx(np.sin(1.0), 0.001)
def test_water_density():
dens = openmc.data.water_density
# These test values are from IAPWS R7-97(2012). They are actually specific
# volumes so they need to be inverted. They also need to be divided by 1000
# to convert from [kg / m^3] to [g / cm^2].
assert dens(300.0, 3.0) == pytest.approx(1e-3/0.100215168e-2, 1e-6)
assert dens(300.0, 80.0) == pytest.approx(1e-3/0.971180894e-3, 1e-6)
assert dens(500.0, 3.0) == pytest.approx(1e-3/0.120241800e-2, 1e-6)