argon.fld

一个关于物性计算的软件

39.948                                 !molecular weight [g/mol]
83.80                                  !triple point temperature [K]
68.906                                 !pressure at triple point [kPa]
35.4                                   !density at triple point [mol/L]
87.302                                 !normal boiling point temperature [K]
-0.002                                 !acentric factor
150.86       4905.8       13.41        !Tc [K], pc [kPa], rhoc [mol/L]
150.86                    13.41        !reducing parameters [K, mol/L]
13.418                                 !gamma
0.0831434                              !gas constant [L-bar/mol-K]
      32       1                       !Nterm, Ncoeff per term
 -0.6569731294d-03     0.1822957801d-00     -0.3649470141d+01
  0.1232012107d+03    -0.8613578274d+04      0.7978579691d-04
 -0.2911489110d-01     0.7581821758d+01      0.8780488169d+04
  0.1423145989d-06     0.1674146131d-02     -0.3200447909d-00
  0.2561766372d-04    -0.5475934941d-03     -0.4505032058d-00
  0.2013254653d-04    -0.1678941273d-06      0.4207329271d-03
 -0.5444212996d-05    -0.8004855011d+04     -0.1319304201d+06
 -0.4954923930d+02     0.8092132177d+05     -0.9870104061d-01
  0.2020441562d+01    -0.1637417205d-03     -0.7038944136d-00
 -0.1154324539d-06     0.1555990117d-04     -0.1492178536d-09
 -0.1001356071d-07     0.2933963216d-06


#AUX               !auxiliary model specification
CP2  ideal gas heat capacity function of Younglove
?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]
600.0              !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
  2.5000000000d+0       0.00d0


#TCX               !thermal conductivity model specification
TC1  pure fluid thermal conductivity model of Lemmon and Jacobsen (2001).
?LITERATURE REFERENCE \
?Lemmon, E.W. and Jacobsen, R.T,
? preliminary equation, 2001.
?\
?The uncertainty in thermal conductivity is 2%.
?\
!end of info section
83.8058            !lower temperature limit [K]
2000.0             !upper temperature limit [K]
1000000.0          !upper pressure limit [kPa]
50.65              !maximum density [mol/L]
2   0              !# terms for dilute gas function:  numerator, denominator
150.687   1.0d-3   !reducing parameters for T, tcx
1.113                    0.0           !coeff, power in T
0.                     -96.0           !coeff, power in T
6   0              !# terms for background gas function:  numerator, denominator
150.687   13.40742965 1.0d-3    !reducing parameters for T, rho, tcx
 0.808988587735E+01   0.3517   1.0000   0.0000     !coeff, powers of t, rho, exp(rho)
 0.282141564450E+02  -0.1308   2.0000   0.0000
-0.177669835303E+01  -4.4438   1.0000   1.0000
-0.668846314430E+02  -0.2799   3.0000   1.0000
 0.226891675451E+02  -1.5418   4.0000   2.0000
 0.940133443986E+01  -8.8969   2.0000   3.0000
TK3                !pointer to critical enhancement auxiliary function


#AUX               !thermal conductivity critical enhancement model
TK3  thermal conductivity critical enhancement of Lemmon and Jacobsen (2001).
?LITERATURE REFERENCE \
?Lemmon, E.W. and Jacobsen, R.T,
? preliminary equation, 2001.
?\
!end of info section
83.8058            !lower temperature limit [K]
2000.0             !upper temperature limit [K]
1000000.0          !upper pressure limit [kPa]
50.65              !maximum density [mol/L]
9  0  0  0         !# terms:  terms, spare, spare, spare
1.0    1.0  1.0    !reducing par for T, rho, tcx (mW/m-K)
0.630d0            !gnu (universal exponent)
1.2415d0           !gamma (universal exponent)
1.01d0             !R0 (universal amplitude)
 0.065d0           !z (universal exponent--not used for t.c., only viscosity)
 1.00d0            !c (constant in viscosity eqn = 1/[2 - (alpha + gamma)/(2*nu)], but often set to 1)
 0.31088466E-09    !xi0 (amplitude) [m]
 0.55000000E-01    !gam0 (amplitude) [-]
 0.51260334E-09    !qd_inverse (modified effective cutoff parameter) [m]
301.374            !tref (reference temperature) [K]


#ETA               !viscosity model specification
VS1  pure fluid viscosity model of Lemmon and Jacobsen (2001).
?LITERATURE REFERENCE \
?Lemmon, E.W. and Jacobsen, R.T,
? preliminary equation, 2001.
?\
?The uncertainty in viscosity is 2%, except in the dilute gas, where the
?uncertainty is 0.5%.
?\
!end of info section
83.8058            !lower temperature limit [K]
2000.0             !upper temperature limit [K]
1000000.0          !upper pressure limit [kPa]
50.65              !maximum density [mol/L]
1                  !number of terms associated with dilute-gas function
CI1                !pointer to reduced effective collision cross-section model
0.3478             !Lennard-Jones coefficient sigma [nm]
104.9              !Lennard-Jones coefficient epsilon/kappa [K]
1.0    1.0         !reducing parameters for T, eta
0.1687292  0.50d0  !Chapman-Enskog term
0                  !number of terms for initial density dependence
0 6 0 0 0 0        !# resid terms:  close-packed density;  simple poly; numerator of rational poly; denominator of rat. poly; numerator of exponential; denominator of exponential
150.687   13.40742965 1.0           !reducing parameters for T, rho, eta
 0.648491572951E+01   0.0000   1.0   0.0   0     !simple polynomial terms
 0.921829714883E+01   0.0000   2.0   0.0   0
 0.251873627628E+01  -1.1303   4.0   0.0   0
 0.710198542697E-01  -0.2879   7.0   0.0   0
 0.233411121182E+00  -4.4346   4.0   0.0   0
-0.365386072189E+01  -2.2411   3.0   0.0   0
NUL                !pointer to critical enhancement auxiliary function (none used)


#AUX               !collision integral specification
CI1  collision integral model of Lemmon and Jacobsen (2001).
?LITERATURE REFERENCE \
?Lemmon, E.W. and Jacobsen, R.T,
? preliminary equation, 2001.
?\
!end of info section
1.0                !lower temperature limit [K]
10000.0            !upper temperature limit [K]
0.0                !(dummy) upper pressure limit
0.0                !(dummy) maximum density
5                  !number of terms
 0.5136E+00 0      !coeff, power of Tstar
-0.5218E+00 1
 0.8852E-01 2
 0.3445E-02 3
-0.2289E-02 4


@ETA               !viscosity model specification
VS3  pure fluid viscosity model of Younglove and Hanley (1986).
?REFERENCE \
?Younglove, B.A. and Hanley, H.J.M.,
? "The Viscosity and Thermal Conductivity Coefficients of Gaseous and
? Liquid Argon,"
? J. Phys. Chem. Ref. Data, 15(4):1323-1337, 1986.
?\
?The uncertainty in viscosity is 2% below 100 MPa and 3% for higher pressures.
?\
!end of info section
55.0               !lower temperature limit [K]
2500.0             !upper temperature limit [K]
1000000.0          !upper pressure limit [kPa]
50.65              !maximum density [mol/L]
9   0              !# terms for dilute gas function:  numerator, denominator
1.0     1.0        !reducing parameters for T, eta
-0.8973188257d5   -1.00d0   !coeff, power in T
 0.8259113473d5   -0.666666666667d0
-0.2766475915d5   -0.333333333333d0
 0.3068539784d4    0.00d0
 0.4553103615d3    0.333333333333d0
-0.1793443839d3    0.666666666667d0
 0.2272225106d2    1.00d0
-0.1350672796d1    1.333333333333d0
 0.3183693230d-1   1.666666666667d0
11  3              !# terms for background gas function:  numerator, denominator
1.0    1.0    1.0                         !reducing par for T, rho (rho_c), eta
 0.5927733783d0    0.00d0   1.00d0   0.   !coeff, powers of t, rho, spare for future use
-0.4251221169d2   -1.00d0   1.00d0   0.
-0.2698477165d-1   0.00d0   2.00d0   0.
 0.3727762288d2   -1.00d0   2.00d0   0.
-0.3958508720d4   -2.00d0   2.00d0   0.
 0.3636730841d-2   0.00d0   3.00d0   0.
-0.2633471347d1   -1.00d0   3.00d0   0.
 0.2936563322d3   -2.00d0   3.00d0   0.
-0.3811869019d-4   0.00d0   4.00d0   0.
 0.4451947464d-1  -1.00d0   4.00d0   0.
-0.5385874487d1   -2.00d0   4.00d0   0.
 1.0000000000      0.00d0   0.00d0   0.
-0.1115054926d-1   0.00d0   1.00d0   0.
-0.1328893444d1   -1.00d0   1.00d0   0.
NUL                !pointer to critical enhancement auxiliary function


@TCX               !thermal conductivity model specification
TC3  pure fluid thermal conductivity model 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
83.8058            !lower temperature limit [K]
600.0              !upper temperature limit [K]
100000.0           !upper pressure limit [kPa]
50.65              !maximum density [mol/L]
0.3297             !Lennard-Jones coefficient sigma [nm]
152.8              !Lennard-Jones coefficient epsilon/kappa [K]
0.16871158559818   !const in Eq 20 = 5/16*(k*MW/1000/pi/Na)**0.5*1.0d12
 0                 !exponent in Eq 20 for T
 2.64712871543D-02 !eta0 (eq 20): coeffs of {(e/kT)**((4-n)/3)}
-.216629583011974
0.709700888884514
-1.21908891344223
 1.20168985706305
-.700084760049098
0.24816605762696
-4.79479287295D-02
 3.93679190444D-03
 9.64428741429D-04 !coeff for initial density dependence of viscosity (eq 21); Fv(1)
 3.02391316601D-04 !Fv(2)
 1                 !Fv(3)
 152.8             !Fv(4)
-33.327027332      !coefficients for residual viscosity, eqs (22 - 25)
-355.59415848      !Ev(2)
 22.2441164817987  !Ev(3)
 1663.62775376509  !Ev(4)
 0                 !Ev(5)
 0                 !Ev(6)
 0                 !Ev(7)
 25.0325423049965  !Ev(8)
 1.7124            !F
0.00000003669      !rm
NUL                !pointer to critical enhancement auxiliary function (none used)


@ETA               !viscosity model specification
VS2  pure fluid viscosity model 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
83.8058            !lower temperature limit [K]
600.0              !upper temperature limit [K]
100000.0           !upper pressure limit [kPa]
50.65              !maximum density [mol/L]
CI2                !pointer to collision integral model
0.3297             !Lennard-Jones coefficient sigma [nm]
152.8              !Lennard-Jones coefficient epsilon/kappa [K]
0.16871158559818   !const in Eq 19 = 5/16*(k*MW/1000/pi/Na)**0.5*1.0d12
 0                 !exponent in Eq 20 for T
 5.85384107393D-03 !coeff for initial density dependence of viscosity (eq 21); Fv(1)
-3.09546765250D-03 !Fv(2)
 1.4               !Fv(3)
 152.8             !Fv(4)
-12.313579086      !coefficients for residual viscosity, eqs (22 - 25)
 40.136071933      !Ev(2)