CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

Nasa Polynomials/ Janf for SES36

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   January 30, 2019, 05:43
Default Nasa Polynomials/ Janf for SES36
  #1
Member
 
Henrik Johansson
Join Date: Oct 2017
Location: Gothenburg
Posts: 38
Rep Power: 8
HenrikJohansson is on a distinguished road
Hi,

I am working for quite some time to simulate an axial turbine with SES36 as real gas.
SES36 is alot like HFC-365mfc.
I think there is something wrong with my Nasa Polynomials because the rothalpy is not correct. Im running foam-extend 4.0.
Below are is my thermiphysicalProperties.

Is this the correct way to calculate the nasa polynomials for a fluid?
I have entropy, enthalpy and constant heat for a range of temperatures.
I then use least square to fit these to the nasa polynomials.

Code:
thermoType      realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<redlichKwong>>>>>;
mixture         SES36 1 184.53 28.5e5 450.7 2111670.0 -9762.24 -83.3023 0.845058 -0.00236983 3.14876e-06 -1.62616e-09 1.42087e-06 0.983296;
Description of coefficients
Code:
// ************************************************************************************************************* //
//   Coefficient:	[J/kmol*K]
//   SES36                		--> Name
//   1							--> number of Moles
//   184.53               		--> Molar mass, (Volume, old) [g/mol]
//   28.5e5	          			--> critical pressure	[Pa]
//   450.7               		--> critical temperatur	[K]
//   99263.04465                --> critical density (only for aungierRedlichKwong)	[Molar Volume] = [Molar Mass] / [Critical Density]
//   0.351             			--> acentric factor  (not needed for redlichKwong but for pengRobinson, aungierRedlichKwong and soaveRedlichKwong )
//   1329.5               		--> constant cp of perfect gas (used for constantHeatCapacity) [J/K]
//   49436.5054 --> 2.849677801e-13     --> 7 heat capacity polynomial coefficents --> NASA Heat Capacity Polynomial
//   1.42087e-6 0.983296                   --> two coefficents for sutherlandRealGasTransport, https://www.cfd-online.com/Forums/openfoam-pre-processing/62178-sutherlandtransport-setting-air.html
I used the following code to get my Nasa Polynomials for different pressures.
Code:
import numpy as np
from scipy.optimize import leastsq
import matplotlib.pyplot as plt
from tabulate import tabulate
np.set_printoptions(threshold=np.nan)
from SES36_Data import R, M, Import_Data, Get_Data_Names
'''
    ***   INPUT  ***
'''
print("Avalibale SES36 data is:")
names = Get_Data_Names()
print(names)
idx = int(input("Select data by number order, etc. 1,2,3...\r\nSelect: "))-1
print(names[idx] + " selected") 
T, Cp, s, h, Delta_Hf_298_15, h_298_15 = Import_Data(names[idx])

''' Sutherland Transport, Calculate the two, (As, Ts), coefficients '''
mu1 = 15.8257e-6  # Pa*s or kg/m*s
T1 = 126          # K @ 11.121bar
mu2 = 14.2570e-6  # Pa*s or kg/m*s
T2 = 102.62       # K @ 3,74bar

'''
    ***   Calculation  ***
'''

''' Sutherland Transport, Calculate the two coefficients '''
def Sutherland_Transport(mu1, T1, mu2, T2):
    ''' Sutherland Transport equation '''
    ''' mu = As * T^(3/2) / (T + Ts) '''
    rootT1 = np.sqrt(T1)
    mu1rootT2 = mu1*np.sqrt(T2)
    mu2rootT1 = mu2*rootT1
    # Calculate TS:
    Ts = (mu2rootT1 - mu1rootT2)/(mu1rootT2/T1 - mu2rootT1/T2)
    # Calculate As:
    As = mu1*(1.0 + Ts/T1)/rootT1
    return Ts, As  

def NASA_POLYNOM_PLOT_9(pars, T):
    a1, a2, a3, a4, a5, a6, a7, b1, b2 = pars
    y1 = a1/T**2 + a2/T + a3 + a4*T + a5*T**2 + a6*T**3 + a7*T**4
    y2 = -a1/T + a2*np.log(T) + a3*T + a4*T**2/2 + a5*T**3/3 + a6*T**4/4 + a7*T**5/5 + b1
    y3 = -a1/(T**2*2) - a2/T + a3*np.log(T) + a4*T + a5*T**2/2 + a6*T**3/3 + a7*T**4/4 + b2
    return np.array([y1, y2, y3])

def NASA_POLYNOM_9(pars, T, Cp, h, s):
    a1, a2, a3, a4, a5, a6, a7, b1, b2 = pars
    F1 = a1/T**2 + a2/T + a3 + a4*T + a5*T**2 + a6*T**3 + a7*T**4 - Cp
    F2 = -a1/T + a2*np.log(T) + a3*T + a4*T**2/2 + a5*T**3/3 + a6*T**4/4 + a7*T**5/5 + b1 - h
    F3 = -a1/(T**2*2) - a2/T + a3*np.log(T) + a4*T + a5*T**2/2 + a6*T**3/3 + a7*T**4/4 + b2 - s
    return np.concatenate((F1, F2, F3))

def Round(var):
    form = '5g'
    if var.size > 1:
        for i in range(0,var.size):
            var[i] = format(var[i], form)
    else:
        var = format(var, form)
    return var

''' Solve the Sutherland Transport equation '''

Ts, As = Sutherland_Transport(mu1, T1, mu2, T2)
print('\r\nSutherland Transport constants:\r\n\r\nAs = {0}\r\nTs = {1}\r\n'.format(Round(As),Round(Ts)))
#print(As * T1**(3/2) / (T1 + Ts))
#print(As * T2**(3/2) / (T2 + Ts))

''' Solve NASA Polynomials '''

# initial values 
par_init = np.zeros(9)
h = Delta_Hf_298_15 + h - h_298_15    # H(T) = Delta Hf(298) + [ H(T) - H(298) ]
best, cov, info, message, ier = leastsq(NASA_POLYNOM_9,
                                        par_init, args=(T, Cp/R, h/R, s/R),
                                        full_output=True)

print('\n\r{0}\r\n'.format(message))

'''
    ***   Print Result  ***
'''

y_calc1, y_calc2, y_calc3 = NASA_POLYNOM_PLOT_9(best, T) * R
best = Round(best)
print(tabulate( [best], headers=['a1', 'a2', 'a3', 'a4', 'a5', 'a6', 'a7', 'b1', 'b2']))
print('\r\n{0} {1} {2} {3} {4} {5} {6}\r\n'.format(best[0], best[1], best[2], best[3], best[4], best[5], best[6]))
fig, (ax1, ax2, ax3) = plt.subplots(1, 3, figsize=(12, 6), dpi=80, facecolor='w', edgecolor='k')
fig.subplots_adjust(left=0.05, bottom=None, right=0.98, top=None, wspace=None, hspace=None)
ax1.plot(T, Cp,'or', label = 'Input') 
ax1.plot(T, y_calc1, label = 'Leastsq')
ax1.set_title('Cp')
ax1.legend(loc=4)
ax2.plot(T, h, 'or', label = 'Input')
ax2.plot(T, y_calc2, label = 'Leastsq')
ax2.set_title('h')
ax2.legend(loc=4)
ax3.plot(T, s, 'or', label = 'Input')
ax3.plot(T, y_calc3, label = 'Leastsq')
ax3.set_title('s')
ax3.legend(loc=4)
plt.show()
SES36_Data.py file
Code:
import numpy as np
# -----------------------------------------------------------------------------------
'''
    ***   11.12 bar Isobar  ***
'''
# -----------------------------------------------------------------------------------
def Isobar11_12(select):
	if select == "data":
		T = np.arange(125, 230, 5) + 273.15 # K

		Cp = np.array([1.3293,1.3107,1.2943,1.283,1.2753,1.2702,1.267,1.2652,
                     1.2647,1.265,1.266,1.2676,1.2697,1.2723,1.2751,1.2782,
                     1.2815,1.285,1.2887,1.2925,1.2964
                     ]) * 1e-3 * M  # J/kmol*K

		s = np.array([1.6568,1.67,1.6861,1.7018,1.7172,1.7323,1.7472,1.7619,
                    1.7764,1.7908,1.805,1.819,1.8329,1.8467,1.8604,1.874,
                    1.8874,1.9008,1.914,1.9272,1.9402
                    ]) * 1e-3 * M # J/kmol*K

		h = np.array([439.02,444.32,450.83,457.27,463.67,470.03,476.37,482.7,
                    489.03,495.35,501.68,508.01,514.35,520.71,527.08,533.46,
                    539.86,546.28,552.71,559.16,565.64
                    ]) *1e-3 * M # J/kmol

		Delta_Hf_298_15 = 96.48 *1e-3 * M     # J/kmol  <-- Heat of formation
		h_298_15 = 435.12 *1e-3 * M            # J/kmol
		return T, Cp, s, h, Delta_Hf_298_15, h_298_15
	elif select == "name":
		return "Isobar 11.12"
	else:
		print("Somthing went wrong with getting data/ name from" + Isobar11_12("name"))
# -----------------------------------------------------------------------------------
'''
    ***   10 bar Isobar  ***
'''
# -----------------------------------------------------------------------------------
def Isobar10(select):
	if select == "data":
		T = np.arange(120, 230, 5) + 273.15 # K

		Cp = np.array([1.286,1.2726,1.2615,1.254,1.2492,1.2464,1.2451,1.2449,
                     1.2456,1.2471,1.2491,1.2516,1.2544,1.2576,1.2611,1.2647,
                     1.2686,1.2726,1.2767,1.2809,1.2852,1.2896
                     ]) * 1e-3 * M  # J/kmol*K

		s = np.array([1.6505,1.664,1.6798,1.6953,1.7105,1.7256,1.7404,1.755,
                    1.7694,1.7837,1.7979,1.8119,1.8258,1.8396,1.8533,1.8669,
                    1.8803,1.8937,1.9069,1.9201,1.9332,1.9462
                    ]) * 1e-3 * M # J/kmol*K

		h = np.array([435.11,440.47,446.8,453.09,459.35,465.59,471.81,478.04,
                    484.26,490.5,496.74,502.99,509.25,515.53,521.83,528.14,
                    534.48,540.83,547.2,553.6,560.01,566.45
                    ]) *1e-3 * M # J/kmol

		Delta_Hf_298_15 = 96.48 *1e-3 * M     # J/kmol  <-- Heat of formation
		h_298_15 = 435.12 *1e-3 * M            # J/kmol
		return T, Cp, s, h, Delta_Hf_298_15, h_298_15
	elif select == "name":
		return "Isobar10"
	else:
		print("Somthing went wrong with getting data/ name from" + Isobar10("name"))

# -----------------------------------------------------------------------------------
'''
    ***   5 bar Isobar  ***
'''
# -----------------------------------------------------------------------------------
def Isobar5(select):
	if select == "data":
		T = np.arange(90, 230, 5) + 273.15 # K


		Cp = np.array([1.1051, 1.1081, 1.1121, 1.1167, 1.1217, 1.1271, 1.1328, 1.1386, 1.1446,
					   1.1507, 1.1569, 1.1632, 1.1695, 1.1758, 1.1822, 1.1885, 1.1949, 1.2012,
					   1.2075, 1.2137, 1.2199, 1.2261, 1.2323, 1.2384, 1.2444, 1.2504, 1.2564,
					   1.2623]) * 1e-3 * M  # J/kmol*K

		s = np.array([1.6115, 1.6257, 1.6407, 1.6555, 1.6702, 1.6848, 1.6993, 1.7136, 1.7279,
					  1.7420, 1.7561, 1.7700, 1.7839, 1.7977, 1.8114, 1.8250, 1.8385, 1.8519,
					  1.8653, 1.8786, 1.8918, 1.9049, 1.9180, 1.9310, 1.9439, 1.9567, 1.9695,
					  1.9822]) * 1e-3 * M # J/kmol*K

		h = np.array([410.95, 416.16, 421.71, 427.28, 432.88, 438.50, 444.15, 449.83, 455.54,
					  461.28, 467.05, 472.85, 478.68, 484.54, 490.44, 496.36, 502.32, 508.31,
					  514.33, 520.39, 526.47, 532.58, 538.73, 544.91, 551.11, 557.35, 563.62,
					  569.92]) *1e-3 * M # J/kmol

		Delta_Hf_298_15 = 111.57 *1e-3 * M     # J/kmol  <-- Heat of formation
		h_298_15 = 410.95 *1e-3 * M            # J/kmol
		return T, Cp, s, h, Delta_Hf_298_15, h_298_15
	elif select == "name":
		return "Isobar 5"
	else:
		print("Somthing went wrong with getting data/ name from" + Isobar5("name"))

# -----------------------------------------------------------------------------------
'''
    ***   1 bar Isobar  ***
'''
# -----------------------------------------------------------------------------------
def Isobar1(select):
	if select == "data":
		T = np.arange(40, 230, 5) + 273.15 # K

		Cp = np.array([0.9165, 0.9278, 0.9390, 0.9500, 0.9608, 0.9715, 0.9821,
				       0.9925, 1.0027, 1.0128, 1.0228, 1.0326, 1.0422, 1.0517,
				       1.0611, 1.0704, 1.0795, 1.0884, 1.0973, 1.1060, 1.1146,
				       1.1231, 1.1315, 1.1397, 1.1479, 1.1559, 1.1638, 1.1716,
				       1.1793, 1.1869, 1.1943, 1.2017, 1.2089, 1.2161, 1.2231,
				       1.2301, 1.2369, 1.2437]) * 1e-3 * M  # J/kmol*K

		s = np.array([1.5559, 1.5706, 1.5851, 1.5996, 1.6141, 1.6285, 1.6428,
				      1.6571, 1.6713, 1.6855, 1.6996, 1.7136, 1.7276, 1.7416,
				      1.7554, 1.7693, 1.7830, 1.7967, 1.8103, 1.8239, 1.8374,
				      1.8509, 1.8643, 1.8776, 1.8909, 1.9041, 1.9173, 1.9304,
				      1.9435, 1.9564, 1.9694, 1.9822, 1.9950, 2.0078, 2.0205,
				      2.0331, 2.0457, 2.0582]) * 1e-3 * M # J/kmol*K

		h = np.array([370.03, 374.65, 379.31, 384.04, 388.81, 393.64, 398.53,
				      403.46, 408.45, 413.49, 418.58, 423.72, 428.90, 434.14,
				      439.42, 444.75, 450.13, 455.55, 461.01, 466.52, 472.07,
				      477.66, 483.30, 488.98, 494.70, 500.46, 506.26, 512.10,
				      517.97, 523.89, 529.84, 535.83, 541.86, 547.92, 554.02,
				      560.15, 566.32, 572.52]) *1e-3 * M # J/kmol

		Delta_Hf_298_15 = 129.41 *1e-3 * M     # J/kmol  <-- Heat of formation
		h_298_15 = 365.71 *1e-3 * M            # J/kmol
		return T, Cp, s, h, Delta_Hf_298_15, h_298_15
	elif select == "name":
		return "Isobar 1"
	else:
		print("Somthing went wrong with getting data/ name from" + Isobar1("name"))

# -----------------------------------------------------------------------------------
'''
    ***   0.1 bar Isobar  ***
'''
# -----------------------------------------------------------------------------------
def Isobar0_1(select):
	if select == "data":
		T = np.arange(-20, 230, 5) + 273.15 # K

		Cp = np.array([0.7498, 0.7635, 0.777, 0.7904, 0.8035, 0.8165, 0.8294, 0.842, 0.8545,
				       0.8668, 0.879, 0.891, 0.9028, 0.9144, 0.9259, 0.9372, 0.9484, 0.9594,
				       0.9703, 0.981, 0.9915, 1.0019, 1.0122, 1.0223, 1.0323, 1.0421, 1.0518,
				       1.0613, 1.0708, 1.08, 1.0892, 1.0982, 1.1071, 1.1159, 1.1245, 1.133,
				       1.1414, 1.1497, 1.1578, 1.1658, 1.1737, 1.1815, 1.1892, 1.1968, 1.2042,
				       1.2116, 1.2188, 1.2259, 1.2329, 1.2398]) * 1e-3 * M  # J/kmol*K

		s = np.array([1.4887, 1.5035, 1.5183, 1.533, 1.5477, 1.5624, 1.5771, 1.5917, 1.6063,
				      1.6209, 1.6354, 1.6499, 1.6643, 1.6787, 1.693, 1.7074, 1.7216, 1.7358,
				      1.75, 1.7641, 1.7782, 1.7922, 1.8061, 1.82, 1.8339, 1.8477, 1.8615,
				      1.8752, 1.8888, 1.9024, 1.9159, 1.9294, 1.9428, 1.9562, 1.9695, 1.9828,
				      1.996, 2.0091, 2.0222, 2.0353, 2.0482, 2.0612, 2.074, 2.0868, 2.0996,
				      2.1123, 2.1249, 2.1375, 2.15, 2.1625]) * 1e-3 * M # J/kmol*K

		h = np.array([322.43, 326.21, 330.06, 333.98, 337.97, 342.02, 346.13, 350.31, 354.55,
				      358.86, 363.22, 367.65, 372.13, 376.67, 381.27, 385.93, 390.65, 395.42,
				      400.24, 405.12, 410.05, 415.03, 420.07, 425.15, 430.29, 435.48, 440.71,
				      445.99, 451.32, 456.7, 462.13, 467.59, 473.11, 478.66, 484.27, 489.91,
				      495.6, 501.32, 507.09, 512.9, 518.75, 524.64, 530.57, 536.53, 542.53,
				      548.57, 554.65, 560.76, 566.91, 573.09]) *1e-3 * M # J/kmol

		Delta_Hf_298_15 = 142.49 *1e-3 * M     # J/kmol  <-- Heat of formation
		h_298_15 = 321.16 *1e-3 * M            # J/kmol
		return T, Cp, s, h, Delta_Hf_298_15, h_298_15
	elif select == "name":
		return "Isobar 0.1"
	else:
		print("Somthing went wrong with getting data/ name from" + Isobar0_1("name"))
# -----------------------------------------------------------------------------------
'''
    ***   Import Data  ***
'''
# -----------------------------------------------------------------------------------

def Import_Data(name):
   if name == Isobar11_12("name"):
       return Isobar11_12("data")
   elif name == Isobar10("name"):
       return Isobar10("data")
   elif name == Isobar5("name"):
       return Isobar5("data")
   elif name == Isobar1("name"):
       return Isobar1("data")
   elif name == Isobar0_1("name"):
       return Isobar0_1("data")
   else:
       print("\n\r Error!   Name does not exist! Could not import data.\n\r")

def Get_Data_Names():
	return Isobar11_12("name"), Isobar10("name"), Isobar5("name"), Isobar1("name"), Isobar0_1("name")

'''
    ***   Gas Properties  ***
'''
R = 8.314472e-3   # J/kmol*K
M = 184.53     # kg/kmol
__________________
/ Henrik Johansson

Last edited by HenrikJohansson; January 30, 2019 at 06:56.
HenrikJohansson is offline   Reply With Quote

Old   January 8, 2020, 04:21
Default
  #2
New Member
 
Join Date: Mar 2017
Posts: 25
Rep Power: 9
.bastian is on a distinguished road
Quote:
Originally Posted by HenrikJohansson View Post
[...]
I have entropy, enthalpy and constant heat for a range of temperatures.
[...]
Where did you take the data from?
Because CoolProp gives different values.
Using the example of the heat capacity for the 1 bar isobar:

Your values:
Code:
Cp = array([0.16941502, 0.17150383, 0.17357415, 0.1756075 , 0.17760388,
            0.17958177, 0.18154119, 0.18346363, 0.18534909, 0.18721608,
            0.18906458, 0.19087611, 0.19265067, 0.19440674, 0.19614433,
            0.19786344, 0.19954557, 0.20119074, 0.20283591, 0.2044441 ,
            0.20603381, 0.20760503, 0.20915777, 0.21067354, 0.21218931,
            0.21366811, 0.21512843, 0.21657026, 0.21799361, 0.21939847,
            0.22076635, 0.22213424, 0.22346517, 0.22479608, 0.22609004,
              0.22738399, 0.22864097, 0.22989795]) # J/kmol*K
CoolProp (CP.PropsSI("CPMOLAR", "T", T, "P", 1e5, "SES36")*1e-3):
Code:
Cp = array([0.14436495, 0.14673565, 0.14921751, 0.15180839, 0.15450591,
            0.15730744, 0.1602101 , 0.16321083, 0.16630641, 0.16949345,
            0.17276842, 0.17612771, 0.17956763, 0.1830844 , 0.18667425,
            0.19033333, 0.19405783, 0.19784394, 0.20168785, 0.20558583,
            0.20953415, 0.21352918, 0.21756733, 0.22164509, 0.22575902,
            0.22990578, 0.23408211, 0.23828485, 0.24251091, 0.24675733,
            0.25102123, 0.25529983, 0.25959046, 0.26389054, 0.26819758,
             0.27250922, 0.27682317, 0.28113724]) # J/kmol*K
Accordingly, this could already be the source of the error.
.bastian is offline   Reply With Quote

Old   April 9, 2021, 03:10
Default
  #3
Member
 
Henrik Johansson
Join Date: Oct 2017
Location: Gothenburg
Posts: 38
Rep Power: 8
HenrikJohansson is on a distinguished road
Hi .bastian,

Thank you for the input.

The data is from Solkane 9. Software supplied by the manufacturerer Solkatherm of SES36.
The rothalpy problem as I now understand it is a problem from the Mixing Plane.

I have started this old project again and will update here when I have found a solution or any other problem regarding the NASA Polynomials
__________________
/ Henrik Johansson
HenrikJohansson is offline   Reply With Quote

Reply

Tags
eos, janf, nasa, polynomials, ses36


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
therm.dat NASA polynomials mystix OpenFOAM 5 May 31, 2018 03:17
NASA Polynomials >> UNITS << Tobi Main CFD Forum 11 February 23, 2017 13:47
Ansys CFX problem: unexpected very high temperatures in premix laminar combustion faizan_habib7 CFX 4 February 1, 2016 17:00
nasa polynomials gardian CFX 3 March 10, 2011 06:29
NASA polynomials, thermo.dat tables Tomislav Sencic Main CFD Forum 8 December 15, 2009 10:09


All times are GMT -4. The time now is 12:36.