1037 lines
51 KiB
Plaintext
1037 lines
51 KiB
Plaintext
Argon !Short name
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7440-37-1 !CAS number
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Argon !Full name
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Ar !Chemical formula {Ar}
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R-740 !Synonym
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39.948 !Molar mass [g/mol]
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83.8058 !Triple point temperature [K]
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87.302 !Normal boiling point [K]
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150.687 !Critical temperature [K]
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4863.0 !Critical pressure [kPa]
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13.4074 !Critical density [mol/L]
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-0.00219 !Acentric factor
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0.0 !Dipole moment [Debye]; (exactly zero for monatomic molecules)
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OT0 !Default reference state
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298.15 101.325 6197.0 154.737 !Tref, Pref, Href, Sref
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10.0 !Version number
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1951 !UN Number :UN:
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cryogen !Family :Family:
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0.0 !Heating value (upper) [kJ/mol] :Heat:
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A1 !Safety Group (ASHRAE Standard 34, 2010) :Safety:
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1S/Ar !Standard InChI String :InChi:
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XKRFYHLGVUSROY-UHFFFAOYSA-N !Standard InChI Key :InChiKey:
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edbdc8e0 (nitrogen) !Alternative fluid for mixing rules :AltID:
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ed016370 !Hash number from InChI Key :Hash:
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!The fluid files contain general information about the fluid in the first 15 to 20 lines, followed by sections for the
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! equations of state, transport equations, and auxiliary equations. Equations of state are listed first. The NIST recommended
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! equations begin with a hash mark (#). The secondary equations begin with the @ symbol. These symbols can be swapped to
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! select a secondary equation as primary and the primary as secondary. The equation of state section also contains auxiliary
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! equations for the ideal gas heat capacity or ideal gas Helmholtz energy. Below the equations of state (both primary and
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! secondary) are the transport equations, first viscosity and then thermal conductivity. These are then followed by the
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! secondary equations if available. The transport section also contains auxiliary equations required to calculate either the
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! dilute gas state or the critical enhancement. At the end of the file are additional but not necessary auxiliary equations,
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! including simple equations for the vapor pressure, saturated liquid and vapor densities, melting line (for some fluids), and
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! sublimation line (for even fewer fluids). This section also contains the equations for dielectric constant and surface
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! tension if available. The sections are divided by different symbols (these being _-+=^*~) to aid the eye in locating a
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! particular section. Secondary equations are indented 10 spaces to avoid confusion with the NIST recommended equations. The
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! end of the fluid file is marked with @END. Anything below that is ignored.
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! compiled by E.W. Lemmon, NIST Physical and Chemical Properties Division, Boulder, Colorado
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! 12-03-97 EWL, Original version.
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! 06-23-98 EWL, Add Tegeler equation of state as default equation.
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! 06-24-98 EWL, Add Younglove BWR equation.
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! 06-26-98 EWL, Add Younglove transport equations.
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! 01-07-99 EWL, Change ECS reference fluid to nitrogen.
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! 10-27-99 EWL, Add Span 12 term equation.
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! 11-15-99 EWL, Change default reference state.
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! 03-20-00 EWL, Change max density to the density at p=2*pmax along melting line.
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! 05-20-01 EWL, Add sublimation line.
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! 11-26-02 EWL, Change reference state to OT0 with values from CODATA.
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! 06-10-03 EWL, Finalize transport equations.
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! 08-05-04 EWL, Add Harvey and Lemmon dielectric correlation.
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! 11-18-04 MLH, Add tPR.
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! 09-14-06 EWL, Change upper T limit from 700 to 2000 K.
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! 12-02-06 MLH, Update LJ for ECS.
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! 06-10-10 CKL, Add ancillary equations.
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! 12-06-12 EWL, Add surface tension coefficients of Mulero et al. (2012).
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________________________________________________________________________________
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#EOS !---Equation of state---
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FEQ !Helmholtz equation of state for argon of Tegeler et al. (1999).
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:TRUECRITICALPOINT: 150.687 13.40742965 !True EOS critical point [K, mol/L] (where dP/dD=0 and d^2P/dD^2=0 at constant T)
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:DOI: 10.1063/1.556037
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Tegeler, Ch., Span, R., and Wagner, W.,
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? "A New Equation of State for Argon Covering the Fluid Region for
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? Temperatures from the Melting Line to 700 K at Pressures up to 1000 MPa,"
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? J. Phys. Chem. Ref. Data, 28(3):779-850, 1999.
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?
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?The estimated uncertainty in density is less than 0.02% for pressures up
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? to 12 MPa and temperatures up to 340 K with the exception of the
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? critical region and less than 0.03% for pressures up to 30 MPa and
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? temperatures between 235 and 520 K. Elsewhere, the uncertainty in
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? density is generally within 0.2%. In the region with densities up to
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? half the critical density and for temperatures between 90 and 450 K, the
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? estimated uncertainty of calculated speeds of sound is in general less
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? than 0.02%. In the liquid and supercritical regions, the uncertainty is
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? less than 1%. The uncertainty in heat capacities is within 0.3% for the
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? vapor and 2% for the liquid. The formulation gives reasonable
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? extrapolation behavior up to very high pressures (50 GPa) and
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? temperatures (17000 K).
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?
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!```````````````````````````````````````````````````````````````````````````````
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83.8058 !Lower temperature limit [K]
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2000.0 !Upper temperature limit [K]
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1000000.0 !Upper pressure limit [kPa]
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50.65 !Maximum density [mol/L]
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CPP !Pointer to Cp0 model
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39.948 !Molar mass [g/mol]
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83.8058 !Triple point temperature [K]
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68.891 !Pressure at triple point [kPa]
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35.465 !Density at triple point [mol/L]
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87.302 !Normal boiling point temperature [K]
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-0.00219 !Acentric factor
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150.687 4863.0 13.40742965 !Tc [K], pc [kPa], rhoc [mol/L]
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150.687 13.40742965 !Reducing parameters [K, mol/L]
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8.31451 !Gas constant [J/mol-K]
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37 4 4 12 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
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0.08872230499 0.0 1. 0. !a(i),t(i),d(i),l(i)
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0.705148051673 0.25 1. 0.
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-1.68201156541 1.0 1. 0.
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-0.149090144315 2.75 1. 0.
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-0.120248046009 4.0 1. 0.
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-0.121649787986 0.0 2. 0.
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0.400359336268 0.25 2. 0.
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-0.271360626991 0.75 2. 0.
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0.242119245796 2.75 2. 0.
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0.00578895831856 0.0 3. 0.
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-0.0410973356153 2.0 3. 0.
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0.0247107615416 0.75 4. 0.
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-0.321813917507 3.0 1. 1.
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0.332300176958 3.5 1. 1.
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0.0310199862873 1.0 3. 1.
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-0.0307770860024 2.0 4. 1.
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0.0938911374196 4.0 4. 1.
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-0.090643210682 3.0 5. 1.
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-0.000457783492767 0.0 7. 1.
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-0.826597290252e-4 0.5 10. 1.
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0.000130134156031 1.0 10. 1.
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-0.011397840002 1.0 2. 2.
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-0.0244551699605 7.0 2. 2.
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-0.064324067176 5.0 4. 2.
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0.0588894710937 6.0 4. 2.
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-0.00064933552113 6.0 8. 2.
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-0.0138898621584 10.0 3. 3.
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0.404898392969 13.0 5. 3.
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-0.386125195947 14.0 5. 3.
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-0.188171423322 11.0 6. 3.
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0.159776475965 14.0 6. 3.
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0.0539855185139 8.0 7. 3.
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-0.028953417958 14.0 7. 3.
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-0.0130254133814 6.0 8. 3.
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0.00289486967758 7.0 9. 3.
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-0.00226471343048 24.0 5. 4.
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0.00176164561964 22.0 6. 4.
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0.00585524544828 3.0 2. 2. 2. -20.0 -250.0 1.11 1.0 0. 0. 0.
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-0.6925190827 1.0 1. 2. 2. -20.0 -375.0 1.14 1.0 0. 0. 0.
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1.53154900305 0.0 2. 2. 2. -20.0 -300.0 1.17 1.0 0. 0. 0.
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-0.00273804474498 0.0 3. 2. 2. -20.0 -225.0 1.11 1.0 0. 0. 0.
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eta beta gamma epsilon
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EXP[eta*(delta-epsilon)^2+beta*(tau-gamma)^2]
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#AUX !---Auxiliary function for Cp0
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CPP !Ideal gas heat capacity function for argon of Tegeler et al. (1999).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Tegeler, Ch., Span, R., and Wagner, W.,
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? "A New Equation of State for Argon Covering the Fluid Region for
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? Temperatures from the Melting Line to 700 K at Pressures up to 1000 MPa,"
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? J. Phys. Chem. Ref. Data, 28(3):779-850, 1999.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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1.0 8.31451 !Reducing parameters for T, Cp0
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1 0 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
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2.5 0.0
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#AUX !---Auxiliary function for PX0
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PX0 !Helmholtz energy ideal-gas function for argon of Tegeler et al. (1999).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Tegeler, Ch., Span, R., and Wagner, W.,
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? "A New Equation of State for Argon Covering the Fluid Region for
|
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? Temperatures from the Melting Line to 700 K at Pressures up to 1000 MPa,"
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? J. Phys. Chem. Ref. Data, 28(3):779-850, 1999.
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?
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!```````````````````````````````````````````````````````````````````````````````
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1 2 0 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau))
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1.5 1.0 !ai, ti for [ai*log(tau**ti)] terms
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-10.2938148004759711 0.0 !aj, ti for [ai*tau**ti] terms
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-0.0003415237881503 1.0 !aj, ti for [ai*tau**ti] terms
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#AUX !---Auxiliary function for PH0
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PH0 !Ideal gas Helmholtz form for argon.
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Tegeler, Ch., Span, R., and Wagner, W.,
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? "A New Equation of State for Argon Covering the Fluid Region for
|
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? Temperatures from the Melting Line to 700 K at Pressures up to 1000 MPa,"
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? J. Phys. Chem. Ref. Data, 28(3):779-850, 1999.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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1 2 0 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau)); cosh; sinh
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1.5 1.0 !ai, ti for [ai*log(tau**ti)] terms
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-10.2938148005 0.0 !aj, ti for [ai*tau**ti] terms
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-0.0003415238 1.0
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--------------------------------------------------------------------------------
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@EOS !---Equation of state---
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FEK !Helmholtz equation of state for argon of Kunz and Wagner (2004).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
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? "The GERG-2004 Wide-Range Equation of State for Natural Gases
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? and Other Mixtures," GERG Technical Monograph 15,
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? Fortschritt-Berichte VDI, VDI-Verlag, Düsseldorf, 2007.
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?
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!```````````````````````````````````````````````````````````````````````````````
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83.8058 !Lower temperature limit [K]
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700.0 !Upper temperature limit [K]
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1000000.0 !Upper pressure limit [kPa]
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50.65 !Maximum density [mol/L]
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PHK !Pointer to Cp0 model
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39.948 !Molar mass [g/mol]
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83.8058 !Triple point temperature [K]
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69.03 !Pressure at triple point [kPa]
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35.5 !Density at triple point [mol/L]
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87.29 !Normal boiling point temperature [K]
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-0.0006 !Acentric factor
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150.687 4879.8 13.407429659 !Tc [K], pc [kPa], rhoc [mol/L]
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150.687 13.407429659 !Reducing parameters [K, mol/L]
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8.314472 !Gas constant [J/mol-K]
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12 4 0 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
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0.85095714803969 0.250 1. 0.
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-2.4003222943480 1.125 1. 0.
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0.54127841476466 1.5 1. 0.
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0.016919770692538 1.375 2. 0.
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0.068825965019035 0.25 3. 0.
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0.00021428032815338 0.875 7. 0.
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0.17429895321992 0.625 2. 1.
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-0.033654495604194 1.75 5. 1.
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-0.13526799857691 3.625 1. 2.
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-0.016387350791552 3.625 4. 2.
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-0.024987666851475 14.5 3. 3.
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0.0088769204815709 12.0 4. 3.
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@AUX !---Auxiliary function for PH0
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PHK !Ideal gas Helmholtz form for argon of Kunz and Wagner (2004).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Kunz, O., Klimeck, R., Wagner, W., Jaeschke, M.
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? "The GERG-2004 Wide-Range Equation of State for Natural Gases
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? and Other Mixtures," GERG Technical Monograph 15,
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? Fortschritt-Berichte VDI, VDI-Verlag, Düsseldorf, 2007.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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1 2 0 0 0 0 0 0 !Nterms: ai*log(tau**ti); ai*tau**ti; ai*log(1-exp(bi*tau)); cosh; sinh
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1.5 1.0 !ai, ti for [ai*log(tau**ti)] terms
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8.3166315 0.0 !aj, ti for [ai*tau**ti] terms
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-4.9465026 1.0
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@EOS !---Equation of state---
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FE1 !Helmholtz equation of state for argon of Stewart and Jacobsen (1989).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Stewart, R.B. and Jacobsen, R.T,
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? "Thermodynamic Properties of Argon from the Triple Point to 1200 K at
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? Pressures to 1000 MPa,"
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? J. Phys. Chem. Ref. Data, 18(2):639-798, 1989.
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?
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!```````````````````````````````````````````````````````````````````````````````
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83.804 !Lower temperature limit [K]
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1200.0 !Upper temperature limit [K]
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1000000.0 !Upper pressure limit [kPa]
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45.814 !Maximum density [mol/L]
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CP1 !Pointer to Cp0 model
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39.948 !Molar mass [g/mol]
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83.804 !Triple point temperature [K]
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68.961 !Pressure at triple point [kPa]
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35.475 !Density at triple point [mol/L]
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87.293 !Normal boiling point temperature [K]
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-0.004 !Acentric factor
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150.6633 4860.0 13.29 !Tc [K], pc [kPa], rhoc [mol/L]
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150.6633 13.29 !Reducing parameters [K, mol/L]
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8.31434 !Gas constant [J/mol-K]
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28 4 0 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
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0.7918675715 0.25 1. 0. !a(i),t(i),d(i),l(i)
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-1.633346151 1.0 1. 0.
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-0.439530293 3.0 1. 0.
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0.1033899999 4.0 1. 0.
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0.2061801664 0.25 2. 0.
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-0.2888681776 1.0 2. 0.
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0.439801055 2.5 2. 0.
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-0.08429550391 3.5 2. 0.
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-0.2155658654 0.75 3. 0.
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0.4786509099 1.0 3. 0.
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-0.3525884593 1.5 3. 0.
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0.03015073692 2.5 3. 0.
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0.02987679059 1.0 4. 0.
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-0.01522568583 2.0 4. 0.
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0.0007435785786 2.0 6. 0.
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0.07099541624 5.0 1. 3.
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-0.02904237185 7.0 1. 3.
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-0.06223078525 5.0 2. 2.
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0.0001410895187 22.0 2. 4.
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-0.001481241783 16.0 2. 6.
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0.03023342784 10.0 3. 3.
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-0.06126784685 14.0 3. 3.
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0.0270996709 16.0 3. 3.
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0.09411034405 4.0 4. 2.
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-0.007291645114 8.0 4. 2.
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-0.001586314976 10.0 4. 4.
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0.0009510948813 5.0 8. 2.
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0.0007786181844 6.0 8. 2.
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@AUX !---Auxiliary function for Cp0
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CP1 !Ideal gas heat capacity function for argon.
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?
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?```````````````````````````````````````````````````````````````````````````````
|
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?Stewart, R.B. and Jacobsen, R.T,
|
|
? "Thermodynamic Properties of Argon from the Triple Point to 1200 K at
|
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? Pressures to 1000 MPa,"
|
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? J. Phys. Chem. Ref. Data, 18(2):639-798, 1989. doi: 10.1063/1.555829
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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1.0 8.31434 !Reducing parameters for T, Cp0
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1 0 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
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2.5 0.0
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@EOS !---Equation of state---
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FES !Helmholtz equation of state for argon of Span and Wagner (2003).
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?
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?```````````````````````````````````````````````````````````````````````````````
|
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?Span, R. and Wagner, W.
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? "Equations of State for Technical Applications. II. Results for Nonpolar Fluids,"
|
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? Int. J. Thermophys., 24(1):41-109, 2003. doi: 10.1023/A:1022310214958
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?
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?The uncertainties of the equation of state are approximately 0.2% (to
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? 0.5% at high pressures) in density, 1% (in the vapor phase) to 2% in
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? heat capacity, 1% (in the vapor phase) to 2% in the speed of sound, and
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? 0.2% in vapor pressure, except in the critical region.
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?
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!```````````````````````````````````````````````````````````````````````````````
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83.8058 !Lower temperature limit [K]
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600.0 !Upper temperature limit [K]
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100000.0 !Upper pressure limit [kPa]
|
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50.65 !Maximum density [mol/L]
|
|
CPP !Pointer to Cp0 model
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|
39.948 !Molar mass [g/mol]
|
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83.8058 !Triple point temperature [K]
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69.026 !Pressure at triple point [kPa]
|
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35.498 !Density at triple point [mol/L]
|
|
87.289 !Normal boiling point temperature [K]
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-0.002 !Acentric factor
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150.687 4863.0 13.40743 !Tc [K], pc [kPa], rhoc [mol/L]
|
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150.687 13.40743 !Reducing parameters [K, mol/L]
|
|
8.31451 !Gas constant [J/mol-K]
|
|
12 4 0 0 0 0 0 0 0 0 0 0 !# terms and # coefs/term for normal terms, Gaussian terms, and Gao terms
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|
0.85095715 0.25 1. 0. !a(i),t(i),d(i),l(i)
|
|
-2.4003223 1.125 1. 0.
|
|
0.54127841 1.5 1. 0.
|
|
0.016919771 1.375 2. 0.
|
|
0.068825965 0.25 3. 0.
|
|
0.00021428033 0.875 7. 0.
|
|
0.17429895 0.625 2. 1.
|
|
-0.033654496 1.75 5. 1.
|
|
-0.135268 3.625 1. 2.
|
|
-0.016387351 3.625 4. 2.
|
|
-0.024987667 14.5 3. 3.
|
|
0.0088769205 12.0 4. 3.
|
|
|
|
|
|
@EOS !---Equation of state---
|
|
BWR !MBWR equation of state for argon of Younglove (1982).
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?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.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
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
|
|
39.948 !Molar mass [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
|
|
-0.0006569731294 0.1822957801 -3.649470141
|
|
123.2012107 -8613.578274 0.7978579691e-4
|
|
-0.0291148911 7.581821758 8780.488169
|
|
0.1423145989e-6 0.001674146131 -0.3200447909
|
|
0.2561766372e-4 -0.0005475934941 -0.4505032058
|
|
0.2013254653e-4 -0.1678941273e-6 0.0004207329271
|
|
-0.5444212996e-5 -8004.855011 -131930.4201
|
|
-49.5492393 80921.32177 -0.09870104061
|
|
2.020441562 -0.0001637417205 -0.7038944136
|
|
-0.1154324539e-6 0.1555990117e-4 -0.1492178536e-9
|
|
-0.1001356071e-7 0.2933963216e-6
|
|
|
|
|
|
@AUX !---Auxiliary function for Cp0
|
|
CP2 !Ideal gas heat capacity function for argon of Younglove.
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?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.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
0. !
|
|
10000. !
|
|
0. !
|
|
0. !
|
|
1.0 8.31434 !Reducing parameters for T, Cp0
|
|
1 0 0 0 0 0 0 !Nterms: polynomial, exponential, cosh, sinh
|
|
2.5 0.0
|
|
|
|
|
|
@EOS !---Cubic equation of state---
|
|
PRT !Translated Peng-Robinson equation for argon.
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Volume translation of Peng Robinson EOS.
|
|
? Translation computed so that sat. liquid density at Tr=0.7 matches FEQ Helmholtz equation
|
|
? of state for Ar of Tegeler et al. (1999).
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
83.8058 !Lower temperature limit [K]
|
|
2000.0 !Upper temperature limit [K]
|
|
1000000.0 !Upper pressure limit [kPa]
|
|
50.65 !Maximum density [mol/L]
|
|
CPP !Pointer to Cp0 model
|
|
39.948 !Molar mass [g/mol]
|
|
-0.00219 !Acentric factor
|
|
150.687 !Critical temperature [K]
|
|
4863.0 !Critical pressure [kPa]
|
|
13.4074 !Critical density [mol/L]
|
|
8.314472 !Gas constant [J/mol-K]
|
|
1 !Number of parameters
|
|
-0.0034
|
|
|
|
|
|
|
|
|
|
^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^
|
|
|
|
#ETA !---Viscosity---
|
|
VS1 !Pure fluid viscosity model for argon of Lemmon and Jacobsen (2004).
|
|
:DOI: 10.1023/B:IJOT.0000022327.04529.f3
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Lemmon, E.W. and Jacobsen, R.T,
|
|
? "Viscosity and Thermal Conductivity Equations for Nitrogen, Oxygen, Argon, and Air,"
|
|
? Int. J. Thermophys., 25:21-69, 2004.
|
|
?
|
|
?The uncertainty is 0.5% in the dilute gas. Away from the dilute gas
|
|
? (pressures greater than 1 MPa and in the liquid), the uncertainties are
|
|
? as low as 1% between 270 and 300 K at pressures less than 100 MPa, and
|
|
? increase outside that range. The uncertainties are around 2% at
|
|
? temperatures of 180 K and higher. Below this and away from the critical
|
|
? region, the uncertainties steadily increase to around 5% at the triple
|
|
? points of the fluids. The uncertainties in the critical region are
|
|
? higher.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
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
|
|
0.335 !Lennard-Jones coefficient sigma [nm]
|
|
143.2 !Lennard-Jones coefficient epsilon/kappa [K]
|
|
1.0 1.0 !Reducing parameters for T, eta
|
|
0.168729283 0.5 !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
|
|
12.19 -0.42 1. 0. 0 !Simple polynomial terms
|
|
13.99 0.0 2. 0. 0
|
|
0.005027 -0.95 10. 0. 0
|
|
-18.93 -0.5 5. 0. 2
|
|
-6.698 -0.9 1. 0. 4
|
|
-3.827 -0.8 2. 0. 4
|
|
NUL !Pointer to the viscosity critical enhancement auxiliary function (none used)
|
|
|
|
|
|
#AUX !---Auxiliary function for the collision integral
|
|
CI1 !Collision integral model for argon of Lemmon and Jacobsen (2004).
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Lemmon, E.W. and Jacobsen, R.T, 2004.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
0. !
|
|
10000. !
|
|
0. !
|
|
0. !
|
|
5 !Number of terms
|
|
0.431 0 !Coefficient, power of Tstar
|
|
-0.4623 1
|
|
0.08406 2
|
|
0.005341 3
|
|
-0.00331 4
|
|
|
|
|
|
|
|
|
|
================================================================================
|
|
|
|
#TCX !---Thermal conductivity---
|
|
TC1 !Pure fluid thermal conductivity model for argon of Lemmon and Jacobsen (2004).
|
|
:DOI: 10.1023/B:IJOT.0000022327.04529.f3
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Lemmon, E.W. and Jacobsen, R.T,
|
|
? "Viscosity and Thermal Conductivity Equations for Nitrogen, Oxygen, Argon, and Air,"
|
|
? Int. J. Thermophys., 25:21-69, 2004. doi: 10.1023/B:IJOT.0000022327.04529.f3
|
|
?
|
|
?The uncertainty for the dilute gas is 2% with increasing uncertainties
|
|
? near the triple point. For the non-dilute gas, the uncertainty is 2%
|
|
? for temperatures greater than 170 K. The uncertainty is 3% at
|
|
? temperatures less than the critical point and 5% in the critical region,
|
|
? except for states very near the critical point.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
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 0.001 !Reducing parameters for T, tcx
|
|
0.8158 -97.0 !Coefficient, power in T
|
|
-0.4320 0.77
|
|
7 0 !# terms for background gas function: numerator, denominator
|
|
150.687 13.40742965 0.001 !Reducing parameters for T, rho, tcx
|
|
13.73 0. 1. 0. !Coefficient, powers of T, rho, exp(rho)
|
|
10.07 0. 2. 0.
|
|
0.7375 0. 4. 0.
|
|
-33.96 -0.8 5. 2.
|
|
20.47 -1.2 6. 2.
|
|
-2.274 -0.8 9. 2.
|
|
-3.973 -0.5 1. 4.
|
|
TK3 !Pointer to critical enhancement auxiliary function
|
|
|
|
|
|
#AUX !---Auxiliary function for the thermal conductivity critical enhancement
|
|
TK3 !Simplified thermal conductivity critical enhancement for argon of Lemmon and Jacobsen (2004).
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Lemmon, E.W. and Jacobsen, R.T, 2004.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
0. !
|
|
10000. !
|
|
0. !
|
|
0. !
|
|
9 0 0 0 !# terms: terms, spare, spare, spare
|
|
1.0 1.0 1.0 !Reducing parameters for T, rho, tcx [mW/(m-K)]
|
|
0.63 !Nu (universal exponent)
|
|
1.2415 !Gamma (universal exponent)
|
|
1.01 !R0 (universal amplitude)
|
|
0.065 !Z (universal exponent--not used for t.c., only viscosity)
|
|
1.0 !C (constant in viscosity eqn = 1/[2 - (alpha + gamma)/(2*nu)], but often set to 1)
|
|
0.13e-9 !Xi0 (amplitude) [m]
|
|
0.055 !Gam0 (amplitude) [-]
|
|
0.32e-9 !Qd_inverse (modified effective cutoff parameter) [m]
|
|
301.374 !Tref (reference temperature) [K]
|
|
|
|
|
|
|
|
|
|
********************************************************************************
|
|
|
|
@TCX !---Thermal conductivity---
|
|
TC3 !Pure fluid thermal conductivity model for argon of Younglove (1982).
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?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.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
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
|
|
0.0264712871543 !Eta0 (eq 20): coeffs of {(e/kT)**((4-n)/3)}
|
|
-0.216629583011974
|
|
0.709700888884514
|
|
-1.21908891344223
|
|
1.20168985706305
|
|
-0.700084760049098
|
|
0.24816605762696
|
|
-0.0479479287295
|
|
0.00393679190444
|
|
9.64428741429e-4 !Coefficient for initial density dependence of viscosity (eq 21); Fv(1)
|
|
3.02391316601e-4 !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
|
|
TK3 !Pointer to the critical enhancement auxiliary function
|
|
|
|
|
|
@ETA !---Viscosity---
|
|
VS2 !Pure fluid viscosity model for argon of Younglove (1982).
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?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.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
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
|
|
0.0 !Exponent in Eq 20 for T
|
|
0.00585384107393 !Coefficient for initial density dependence of viscosity (eq 21); Fv(1)
|
|
-0.0030954676525 !Fv(2)
|
|
1.4 !Fv(3)
|
|
152.8 !Fv(4)
|
|
-12.313579086 !Coefficients for residual viscosity, eqs (22 - 25)
|
|
40.136071933 !Ev(2)
|
|
11.6160872385243 !Ev(3)
|
|
-413.04094973717 !Ev(4)
|
|
0.0413624595833 !Ev(5)
|
|
7.96883967907912 !Ev(6)
|
|
234.196850483958 !Ev(7)
|
|
13.4424752177831 !Ev(8)
|
|
NUL !Pointer to the viscosity critical enhancement auxiliary function (none used)
|
|
|
|
|
|
@AUX !---Auxiliary function for the collision integral
|
|
CI2 !Collision integral model for argon of Younglove (1982).
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Younglove, B.A. (1982).
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
0. !
|
|
10000. !
|
|
0. !
|
|
0. !
|
|
9 !Number of terms
|
|
25.7830291943396 0 !eta0 (eq 20): coeffs of {(e/kT)**((4-n)/3)}
|
|
-234.320222858983 0
|
|
814.636688705024 0
|
|
-1452.04353466585 0
|
|
1467.17535558104 0
|
|
-870.164951237067 0
|
|
313.024934147423 0
|
|
-61.2072628957372 0
|
|
5.07700488990665 0
|
|
|
|
|
|
|
|
|
|
++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
|
|
|
|
@TRN !---ECS Transport---
|
|
ECS !Extended Corresponding States model (Nitrogen reference); predictive mode for argon.
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Klein, S.A., McLinden, M.O., and Laesecke, A., "An Improved Extended Corresponding States Method for Estimation of Viscosity of Pure Refrigerants and Mixtures," Int. J. Refrigeration, 20(3):208-217, 1997. doi: 10.1016/S0140-7007(96)00073-4.
|
|
?McLinden, M.O., Klein, S.A., and Perkins, R.A., "An Extended Corresponding States Model for the Thermal Conductivity of Refrigerants and Refrigerant Mixtures," Int. J. Refrigeration, 23(1):43-63, 2000. doi: 10.1016/S0140-7007(99)00024-9
|
|
?
|
|
?The Lennard-Jones parameters were taken from Reid, R.C., Prausnitz, J.M., and Poling, B.E., "The Properties of Gases and Liquids," 4th edition, New York, McGraw-Hill Book Company, 1987.
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
83.8058 !Lower temperature limit [K]
|
|
700.0 !Upper temperature limit [K]
|
|
1000000.0 !Upper pressure limit [kPa]
|
|
50.65 !Maximum density [mol/L]
|
|
FEQ NITROGEN.FLD
|
|
VS1 !Model for reference fluid viscosity
|
|
TC1 !Model for reference fluid thermal conductivity
|
|
NUL !Large molecule identifier
|
|
1 !Lennard-Jones flag (0 or 1) (0 => use estimates)
|
|
0.335 !Lennard-Jones coefficient sigma [nm]
|
|
143.2 !Lennard-Jones coefficient epsilon/kappa [K]
|
|
1 0 0 !Number of terms in f_int term in Eucken correlation, spare1, spare2
|
|
0.00132 0. 0. 0. !Coefficient, power of T, spare1, spare2
|
|
1 0 0 !Number of terms in psi (visc shape factor): poly,spare1,spare2
|
|
1.0 0. 0. 0. !Coefficient, power of Tr, power of Dr, spare
|
|
1 0 0 !Number of terms in chi (t.c. shape factor): poly,spare1,spare2
|
|
1.0 0. 0. 0. !Coefficient, power of Tr, power of Dr, spare
|
|
TK3 !Pointer to critical enhancement auxiliary function
|
|
|
|
|
|
|
|
|
|
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
|
|
|
|
#STN !---Surface tension---
|
|
ST1 !Surface tension model for argon of Mulero et al. (2012).
|
|
:DOI: 10.1063/1.4768782
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Mulero, A., Cachadiña, I., and Parra, M.I.,
|
|
? "Recommended Correlations for the Surface Tension of Common Fluids,"
|
|
? J. Phys. Chem. Ref. Data, 41(4), 043105, 2012. doi: 10.1063/1.4768782
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
0. !
|
|
10000. !
|
|
0. !
|
|
0. !
|
|
1 !Number of terms in surface tension model
|
|
150.687 !Critical temperature used in fit (dummy)
|
|
0.037 1.25 !Sigma0 and n
|
|
|
|
|
|
#DE !---Dielectric constant---
|
|
DE3 !Dielectric constant model for argon of Harvey and Lemmon (2005).
|
|
:DOI: 10.1007/s10765-005-2351-5
|
|
?
|
|
?```````````````````````````````````````````````````````````````````````````````
|
|
?Harvey, A.H. and Lemmon, E.W.,
|
|
? "Method for Estimating the Dielectric Constant of Natural Gas Mixtures,"
|
|
? Int. J. Thermophys., 26(1):31-46, 2005. doi: 10.1007/s10765-005-2351-5 doi: 10.1007/s10765-005-2351-5
|
|
?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
|
0. !
|
|
10000. !
|
|
0. !
|
|
0. !
|
|
273.16 1000.0 1.0 !Reducing parameters for T and D
|
|
0 1 3 0 0 0 !Number of terms in dielectric constant model
|
|
4.1414 0. 1. 0. !Coefficient, T exp, D exp
|
|
1.597 0. 2. 0.
|
|
0.262 1. 2. 0.
|
|
-117.9 0. 3.1 0.
|
|
|
|
|
|
#MLT !---Melting line---
|
|
ML1 !Melting line model for argon of Tegeler et al. (1999).
|
|
:DOI: 10.1063/1.556037
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Tegeler, Ch., Span, R., and Wagner, W.,
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? "A New Equation of State for Argon Covering the Fluid Region for
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? Temperatures from the Melting Line to 700 K at Pressures up to 1000 MPa,"
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? J. Phys. Chem. Ref. Data, 28(3):779-850, 1999. doi: 10.1063/1.556037
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?
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!```````````````````````````````````````````````````````````````````````````````
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83.8058 !Lower temperature limit [K]
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700.0 !Upper temperature limit [K]
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0. !
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0. !
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83.8058 68.891 !Reducing temperature and pressure
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5 0 0 0 0 0 !Number of terms in melting line equation
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1.0 0.0 !Coefficients and exponents
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-7476.26651 1.05
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9959.06125 1.275
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7476.26651 0.0
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-9959.06125 0.0
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#SBL !---Sublimation line---
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SB3 !Sublimation line model for argon of Lemmon (2002).
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:DOI:
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Lemmon, E.W., 2002.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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83.8058 !Upper temperature limit [K]
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0. !
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0. !
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83.8058 68.891 !Reducing temperature and pressure
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0 1 0 0 0 0 !Number of terms in sublimation line equation
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-11.1307 1. !Coefficients and exponents
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#PS !---Vapor pressure---
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PS5 !Vapor pressure equation for argon of Tegeler et al. (1999).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Functional Form: P=Pc*EXP[SUM(Ni*Theta^ti)*Tc/T] where Theta=1-T/Tc, Tc and Pc
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? are the reducing parameters below, which are followed by rows containing Ni and ti.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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150.687 4863.0 !Reducing parameters
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4 0 0 0 0 0 !Number of terms in equation
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-5.9409785 1.0
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1.3553888 1.5
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-0.4649761 2.0
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-1.5399043 4.5
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#DL !---Saturated liquid density---
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DL4 !Saturated liquid density equation for argon of Tegeler et al. (1999).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Functional Form: D=Dc*EXP[SUM(Ni*Theta^(ti/3))] where Theta=1-T/Tc, Tc and Dc are
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? the reducing parameters below, which are followed by rows containing Ni and ti.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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150.687 13.40742965 !Reducing parameters
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4 0 0 0 0 0 !Number of terms in equation
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1.5004264 1.002
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-0.3138129 2.0
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0.086461622 7.0
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-0.041477525 12.0
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#DV !---Saturated vapor density---
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DV6 !Saturated vapor density equation for argon of Lemmon (2010).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Equation of Tegeler appears to be wrong, and new equation was fitted here.
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?
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?Functional Form: D=Dc*EXP[SUM(Ni*Theta^(ti/3))*Tc/T] where Theta=1-T/Tc, Tc and Dc are
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? the reducing parameters below, which are followed by rows containing Ni and ti.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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150.687 13.40742965 !Reducing parameters
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4 0 0 0 0 0 !Number of terms in equation
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-1.3721 0.96
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-2.9182 2.16
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0.097930 3.75
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-2.2898 13.02
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@END
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c 1 2 3 4 5 6 7 8
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c2345678901234567890123456789012345678901234567890123456789012345678901234567890
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@TCX !Thermal conductivity model specification
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TC1 pure fluid thermal conductivity model of Younglove and Hanley (1986).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Younglove, B.A. and Hanley, H.J.M.,
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? "The Viscosity and Thermal Conductivity Coefficients of Gaseous and
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? Liquid Argon,"
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? J. Phys. Chem. Ref. Data, 15(4):1323-1337, 1986.
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?
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!```````````````````````````````````````````````````````````````````````````````
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83.8058 !Lower temperature limit [K]
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700.0 !Upper temperature limit [K]
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1000000.0 !Upper pressure limit [kPa]
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50.65 !Maximum density [mol/L]
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9 0 !# terms for dilute gas function: numerator, denominator
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1.0 0.001 !Reducing parameters for T, tcx
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-67009.76192 -1. !Coefficient, power in T
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61522.55283 -0.666666666667
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-20492.18286 -0.333333333333
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2216.966254 0.
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357.9189325 0.333333333333
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-136.4658914 0.666666666667
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17.18671649 1.
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-1.018933154 1.333333333333
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0.02397996932 1.666666666667
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11 3 !# terms for background gas function: numerator, denominator
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1.0 1.0 0.001 !Reducing parameters for T, rho (rho_c), tcx
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1.536300190 0. 1. 0. !Coefficient, powers of T, rho, spare for future use
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-233.2533199 -1. 1. 0.
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-0.03027085824 0. 2. 0.
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18.96279196 -1. 2. 0.
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10.54230664 -2. 2. 0.
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0.2588139028e-4 0. 3. 0.
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-0.4546798772 -1. 3. 0.
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4.320206998 -2. 3. 0.
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0.1593643304e-4 0. 4. 0.
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0.0001262253904 -1. 4. 0.
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-0.002937213042 -2. 4. 0.
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1.0 0. 0. 0.
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-0.02262773007 0. 1. 0.
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-0.1445619495 -1. 1. 0.
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TK4 !Pointer to critical enhancement auxiliary function
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@AUX !---Thermal conductivity critical enhancement model
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TK4 thermal conductivity critical enhancement
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Younglove, B.A. and Hanley, H.J.M., 1986.
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?
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!```````````````````````````````````````````````````````````````````````````````
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0. !
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10000. !
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0. !
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0. !
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6 0 0 0 !# terms
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150.86 4905.8 13.41 0.001 !Reducing parameters for T, rho, tcx [mW/(m-K)]
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1.02
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1.380658e-23
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0.46807
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39.8
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5.45
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0.60795
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@TCX !Thermal conductivity model specification
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TC1 pure fluid thermal conductivity model of Perkins et al. (1991).
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?
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?```````````````````````````````````````````````````````````````````````````````
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?Perkins, R.A., Friend, D.G., Roder, H.M., and Nieto de Castro, C.A.,
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? "Thermal Conductivity Surface of Argon: A Fresh Analysis,"
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? Int. J. Thermophys., 12(6):965-984, 1991. doi: 10.1007/BF00503513
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?
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?The uncertainty in thermal conductivity is 2.2%.
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?
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!```````````````````````````````````````````````````````````````````````````````
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55.0 !Lower temperature limit [K]
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2500.0 !Upper temperature limit [K]
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1000000.0 !Upper pressure limit [kPa]
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50.65 !Maximum density [mol/L]
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9 0 !# terms for dilute gas function: numerator, denominator
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1.0 0.001 !Reducing parameters for T, tcx
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12250.67272 -1. !Coefficient, power in T
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-9096.222831 -0.66666666666666
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2744.958263 -0.33333333333333
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-417.0419051 0.
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25.27591169 0.33333333333333
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1.604421067 0.66666666666666
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-0.2618841031 1.
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0.01381696924 1.33333333333333
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-0.0002463115922 1.66666666666666
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4 0 !# terms for background gas function: numerator, denominator
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1.0 1. 1. !Reducing parameters for T, rho (rho_c), tcx
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0.000757894 0. 1. 0. !Coefficient, powers of T, rho, spare for future use
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0.612624e-4 0. 2. 0.
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-0.205353e-5 0. 3. 0.
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0.745621e-7 0. 4. 0.
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TK4 !Pointer to critical enhancement auxiliary function
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|
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!The following model was moved here on 2/24/2016 because the VS3 model was changed
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! and this one will no longer work with version 9.2 and higher.
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@ETA !Viscosity model specification
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VS3 pure fluid viscosity model of Younglove and Hanley (1986).
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?
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?```````````````````````````````````````````````````````````````````````````````
|
|
?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. doi: 10.1063/1.555765
|
|
?
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?The uncertainty in viscosity is 2% below 100 MPa and 3% for higher pressures.
|
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?
|
|
!```````````````````````````````````````````````````````````````````````````````
|
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55.0 !Lower temperature limit [K]
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|
2500.0 !Upper temperature limit [K]
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|
1000000.0 !Upper pressure limit [kPa]
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|
50.65 !Maximum density [mol/L]
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|
9 0 !# terms for dilute gas function: numerator, denominator
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|
1.0 1.0 !Reducing parameters for T, eta
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|
-89731.88257 -1.0 !Coefficient, power in T
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82591.13473 -0.666666666667
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-27664.75915 -0.333333333333
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3068.539784 0.0
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455.3103615 0.333333333333
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-179.3443839 0.666666666667
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22.72225106 1.0
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-1.350672796 1.333333333333
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0.0318369323 1.666666666667
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11 3 !# terms for background gas function: numerator, denominator
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1.0 1.0 1.0 !Reducing parameters for T, rho (rho_c), eta
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0.5927733783 0. 1. 0. 0 !Coefficient, powers of T, rho, spare for future use
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-42.51221169 -1. 1. 0. 0
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-0.02698477165 0. 2. 0. 0
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37.27762288 -1. 2. 0. 0
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-3958.508720 -2. 2. 0. 0
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0.003636730841 0. 3. 0. 0
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-2.633471347 -1. 3. 0. 0
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293.6563322 -2. 3. 0. 0
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-0.3811869019e-4 0. 4. 0. 0
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0.04451947464 -1. 4. 0. 0
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-5.385874487 -2. 4. 0. 0
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1.0 0. 0. 0. 0
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-0.01115054926 0. 1. 0. 0
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-1.328893444 -1. 1. 0. 0
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TK3 !Pointer to critical enhancement auxiliary function
|
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|
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|