📄 argon.fld
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argon !short name
7440-37-1 !CAS number
argon !full name
Ar !chemical formula
R-740 !synonym
39.948 !molecular weight [g/mol]
83.8058 !triple point temperature [K]
87.302 !normal boiling point [K]
150.687 !critical temperature [K]
4863.0 !critical pressure [kPa]
13.4074 !critical density [mol/L]
-0.00219 !acentric factor
0.0 !dipole moment [Debye]
OTH !default reference state
298.15 100.0 6189.38 154.826 !tref, Pref, Href, Sref
6.1 !version number
! compiled by E.W. Lemmon, NIST Physical and Chemical Properties Division, Boulder, Colorado
! 12-03-97 EWL, original version
! 06-23-98 EWL, added Tegeler equation of state as default equation
! 06-24-98 EWL, add Younglove BWR equation
! 06-26-98 EWL, add Younglove transport equations
! 11-13-98 EWL, update format to version 6.1
! 1-07-99 EWL, change ECS reference fluid to nitrogen
! 10-27-99 EWL, add Span 12 term equation
! 11-15-99 EWL, change default reference state
! 3-20-00 EWL, change max density to the density at p=2*pmax along melting line
! 5-25-00 EWL, drop lower limit on transport eqs. to allow air calculations
! 5-20-01 EWL, add sublimation line
#EOS !equation of state specification
FEQ Helmholtz equation of state for argon of Tegeler et al. (1999).
?LITERATURE REFERENCE \
?Tegeler, Ch., Span, R., and Wagner, W.,
? "A New Equation of State for Argon Covering the Fluid Region for
? Temperatures from the Melting Line to 700 K at Pressures up to 1000 MPa,"
? J. Phys. Chem. Ref. Data, 28(3):779-850, 1999.
?\
?The estimated uncertainty in density is less than 0.02% for pressures up
?to 12 MPa and temperatures up to 340 K with the exception of the
?critical region and less than 0.03% for pressures up to 30 MPa and
?temperatures between 235 and 520 K. Elsewhere, the uncertainty in
?density is generally within 0.2%. In the region with densities up to
?half the critical density and for temperatures between 90 and 450 K, the
?estimated uncertainty of calculated speeds of sound is in general less
?than 0.02%. In the liquid and supercritical regions, the uncertainty is
?less than 1%. The uncertainty in heat capacities is within 0.3% for the
?vapor and 2% for the liquid. The formulation gives reasonable
?extrapolation behavior up to very high pressures (50 GPa) and
?temperatures (17000 K).
?\
!end of info section
83.8058 !lower temperature limit [K]
700.0 !upper temperature limit [K]
1000000.0 !upper pressure limit [kPa]
50.65 !maximum density [mol/L]
CPP !pointer to Cp0 model
39.948 !molecular weight [g/mol]
83.8058 !triple point temperature [K]
68.891 !pressure at triple point [kPa]
35.465 !density at triple point [mol/L]
87.302 !normal boiling point temperature [K]
-0.00219 !acentric factor
150.687 4863.0 13.40742965 !Tc [K], pc [kPa], rhoc [mol/L]
150.687 13.40742965 !reducing parameters [K, mol/L]
8.31451 !gas constant [J/mol-K]
37 4 4 12 0 0 !# terms, # coeff/term for: "normal" terms, critical, spare
0.887223049900d-01 0.000 1.00 0 !a(i),t(i),d(i),l(i)
0.705148051673d+00 0.250 1.00 0
-0.168201156541d+01 1.000 1.00 0
-0.149090144315d+00 2.750 1.00 0
-0.120248046009d+00 4.000 1.00 0
-0.121649787986d+00 0.000 2.00 0
0.400359336268d+00 0.250 2.00 0
-0.271360626991d+00 0.750 2.00 0
0.242119245796d+00 2.750 2.00 0
0.578895831856d-02 0.000 3.00 0
-0.410973356153d-01 2.000 3.00 0
0.247107615416d-01 0.750 4.00 0
-0.321813917507d+00 3.000 1.00 1
0.332300176958d+00 3.500 1.00 1
0.310199862873d-01 1.000 3.00 1
-0.307770860024d-01 2.000 4.00 1
0.938911374196d-01 4.000 4.00 1
-0.906432106820d-01 3.000 5.00 1
-0.457783492767d-03 0.000 7.00 1
-0.826597290252d-04 0.500 10.00 1
0.130134156031d-03 1.000 10.00 1
-0.113978400020d-01 1.000 2.00 2
-0.244551699605d-01 7.000 2.00 2
-0.643240671760d-01 5.000 4.00 2
0.588894710937d-01 6.000 4.00 2
-0.649335521130d-03 6.000 8.00 2
-0.138898621584d-01 10.000 3.00 3
0.404898392969d+00 13.000 5.00 3
-0.386125195947d+00 14.000 5.00 3
-0.188171423322d+00 11.000 6.00 3
0.159776475965d+00 14.000 6.00 3
0.539855185139d-01 8.000 7.00 3
-0.289534179580d-01 14.000 7.00 3
-0.130254133814d-01 6.000 8.00 3
0.289486967758d-02 7.000 9.00 3
-0.226471343048d-02 24.000 5.00 4
0.176164561964d-02 22.000 6.00 4
0.585524544828d-02 3.000 2.00 2 2 -20.0 -250.0 1.11 1. 0. 0. 0.
-0.692519082700d+00 1.000 1.00 2 2 -20.0 -375.0 1.14 1. 0. 0. 0.
0.153154900305d+01 0.000 2.00 2 2 -20.0 -300.0 1.17 1. 0. 0. 0.
-0.273804474498d-02 0.000 3.00 2 2 -20.0 -225.0 1.11 1. 0. 0. 0.
#AUX !auxiliary model specification
CPP ideal gas heat capacity function
?LITERATURE REFERENCE \
?Tegeler, Ch., Span, R., and Wagner, W.,
? "A New Equation of State for Argon Covering the Fluid Region for
? Temperatures from the Melting Line to 700 K at Pressures up to 1000 MPa,"
? J. Phys. Chem. Ref. Data, 28(3):779-850, 1999.
?\
!end of info section
83.8058 !lower temperature limit [K]
700.0 !upper temperature limit [K]
0.0 !upper pressure limit [kPa]
0.0 !maximum density [mol/L]
1.0 8.31451 !reducing parameters for T, Cp0
1 0 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
0.25d1 0.00
@EOS !equation of state specification
FE1 Helmholtz equation of state for argon of Stewart and Jacobsen (1989).
?LITERATURE REFERENCE \
?Stewart, R.B. and Jacobsen, R.T,
? "Thermodynamic Properties of Argon from the Triple Point to 1200 K at
? Pressures to 1000 MPa,"
? J. Phys. Chem. Ref. Data, 18(2):639-798, 1989.
?\
!end of info section
83.804 !lower temperature limit [K]
1200.0 !upper temperature limit [K]
1000000.0 !upper pressure limit [kPa]
45.814 !maximum density [mol/L]
CP1 !pointer to Cp0 model
39.948 !molecular weight [g/mol]
83.804 !triple point temperature [K]
68.961 !pressure at triple point [kPa]
35.475 !density at triple point [mol/L]
87.293 !normal boiling point temperature [K]
-0.004 !acentric factor
150.6633 4860.0 13.29 !Tc [K], pc [kPa], rhoc [mol/L]
150.6633 13.29 !reducing parameters [K, mol/L]
8.31434 !gas constant [J/mol-K]
28 4 0 0 0 0 !# terms, # coeff/term for: "normal" terms, critical, spare
0.791867571500d+00 0.250 1.00 0 !a(i),t(i),d(i),l(i)
-0.163334615100d+01 1.000 1.00 0
-0.439530293000d+00 3.000 1.00 0
0.103389999900d+00 4.000 1.00 0
0.206180166400d+00 0.250 2.00 0
-0.288868177600d+00 1.000 2.00 0
0.439801055000d+00 2.500 2.00 0
-0.842955039100d-01 3.500 2.00 0
-0.215565865400d+00 0.750 3.00 0
0.478650909900d+00 1.000 3.00 0
-0.352588459300d+00 1.500 3.00 0
0.301507369200d-01 2.500 3.00 0
0.298767905900d-01 1.000 4.00 0
-0.152256858300d-01 2.000 4.00 0
0.743578578600d-03 2.000 6.00 0
0.709954162400d-01 5.000 1.00 3
-0.290423718500d-01 7.000 1.00 3
-0.622307852500d-01 5.000 2.00 2
0.141089518700d-03 22.000 2.00 4
-0.148124178300d-02 16.000 2.00 6
0.302334278400d-01 10.000 3.00 3
-0.612678468500d-01 14.000 3.00 3
0.270996709000d-01 16.000 3.00 3
0.941103440500d-01 4.000 4.00 2
-0.729164511400d-02 8.000 4.00 2
-0.158631497600d-02 10.000 4.00 4
0.951094881300d-03 5.000 8.00 2
0.778618184400d-03 6.000 8.00 2
#AUX !auxiliary model specification
CP1 ideal gas heat capacity function
?LITERATURE REFERENCE \
?Stewart, R.B. and Jacobsen, R.T,
? "Thermodynamic Properties of Argon from the Triple Point to 1200 K at
? Pressures to 1000 MPa,"
? J. Phys. Chem. Ref. Data, 18(2):639-798, 1989.
?\
!end of info section
83.804 !lower temperature limit [K]
1200.0 !upper temperature limit [K]
0.0 !upper pressure limit [kPa]
0.0 !maximum density [mol/L]
1.0 8.31434 !reducing parameters for T, Cp0
1 0 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
2.5 0.00
@EOS !equation of state specification
FES short Helmholtz equation of state for argon of Span (2000).
?LITERATURE REFERENCE \
?Span, R.,
? "Multiparameter Equations of State - An Accurate Source of Thermodynamic
? Property Data," Springer, Berlin, Heidelberg, New York, 2000.
?\
?The uncertainties of the equation of state are approximately 0.2% (to
?0.5% at high pressures) in density, 1% (in the vapor phase) to 2% in
?heat capacity, 1% (in the vapor phase) to 2% in the speed of sound, and
?0.2% in vapor pressure, except in the critical region.
?\
!end of info section
83.8058 !lower temperature limit [K]
600.0 !upper temperature limit [K]
100000.0 !upper pressure limit [kPa]
50.65 !maximum density [mol/L]
CPP !pointer to Cp0 model
39.948 !molecular weight [g/mol]
83.8058 !triple point temperature [K]
69.026 !pressure at triple point [kPa]
35.498 !density at triple point [mol/L]
87.289 !normal boiling point temperature [K]
-0.002 !acentric factor
150.687 4863.0 13.40743 !Tc [K], pc [kPa], rhoc [mol/L]
150.687 13.40743 !reducing parameters [K, mol/L]
8.31451 !gas constant [J/mol-K]
12 4 0 0 0 0 !# terms, # coeff/term for: "normal" terms, critical, spare
0.850957150000E+00 0.25 1.0 0 !a(i),t(i),d(i),l(i)
-0.240032230000E+01 1.125 1.0 0
0.541278410000E+00 1.5 1.0 0
0.169197710000E-01 1.375 2.0 0
0.688259650000E-01 0.25 3.0 0
0.214280330000E-03 0.875 7.0 0
0.174298950000E+00 0.625 2.0 1
-0.336544960000E-01 1.75 5.0 1
-0.135268000000E+00 3.625 1.0 2
-0.163873510000E-01 3.625 4.0 2
-0.249876670000E-01 14.5 3.0 3
0.887692050000E-02 12.0 4.0 3
@EOS !equation of state specification
BWR MBWR equation of state for argon of Younglove (1982).
?LITERATURE REFERENCE \
?Younglove, B.A.,
? "Thermophysical Properties of Fluids. I. Argon, Ethylene,
? Parahydrogen, Nitrogen, Nitrogen Trifluoride, and Oxygen,"
? J. Phys. Chem. Ref. Data, Vol. 11, Suppl. 1, pp. 1-11, 1982.
?\
!end of info section
83.80 !lower temperature limit [K]
400.0 !upper temperature limit [K]
101000.0 !upper pressure limit [kPa]
50.65 !maximum density [mol/L]
CP2 !pointer to Cp0 model
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