huber_2018 ========== M\. L\. Huber, "Models for Viscosity, Thermal Conductivity, and Surface Tension of Selected Pure Fluids as Implemented in REFPROP v10\.0", NIST Interagency Report 8209 \(2018\) `Source record `__ · :doc:`Catalogue ` · :doc:`Review register ` DOI: `10\.6028/nist\.ir\.8209 `__ **Source kind:** fit **Recorded technique:** The transport models of REFPROP 10 for fluids without a reference correlation\: extended corresponding states with a reference fluid \(nitrogen for the four gases here\), whose dilute\-gas viscosity is Chapman\-Enskog theory with a Lennard\-Jones collision integral and a correction factor F\_c fitted, per fluid, to dilute\-gas data\. The NIST Chemistry WebBook \(SRD 69\) evaluates these models\. **Materials in structured entries:** Kr, N2O, Ne, Xe **Dataset quantities:** None recorded. **Contents:** 0 datasets; 4 formulas. Curation notes -------------- Identity VALIDATED by the library\. Pages are the report's pdf pages\. THE DILUTE\-GAS VISCOSITY \(pdf p\. 9\)\: Eq\. \(6\), eta\* = 5 sqrt\(m pi k\_B T\) / \(16 pi sigma^2 Omega\(2,2\)\); Eq\. \(7\), Neufeld et al\.'s collision integral without its sinusoidal term, Omega\(2,2\) = 1\.16145 T\*^\-0\.14874 \+ 0\.52487 exp\(\-0\.77320 T\*\) \+ 2\.16178 exp\(\-2\.43787 T\*\), valid for 0\.3 \< T\* \< 100, T\* = k\_B T/epsilon; the dilute viscosity is eta\* times F\_c\. Table 1 \(pdf p\. 262\)\: neon M = 20\.179 g/mol, epsilon/k\_B = 45\.58 K, sigma = 0\.2707 nm; krypton 83\.798, 178\.9 K, 0\.3655 nm; xenon 131\.293, 260\.91 K, 0\.3929 nm; nitrous oxide 44\.0128, 232\.4 K, 0\.3828 nm\. Table 2 \(pdf p\. 265\)\: F\_c = 0\.989544 \(neon\), 1\.008291 \(krypton\), 1\.0012 \(xenon\), 1 \(nitrous oxide\), each with nitrogen as the reference fluid\. All read from the library's tables and text, 2026\-09\-30\. THE CONSTANT\. Table 7's check values of eta\* \(pdf p\. 274\: neon 6\.006075 uPa s at 40 K, krypton 16\.32999 at 188\.5 K, xenon 20\.11099 at 260\.8 K, nitrous oxide 13\.86694 at 278\.6 K\) are reproduced to 2\.4e\-7 by eta\* = 0\.026692 sqrt\(M T\)/\(sigma^2 Omega\) uPa s \(M in g/mol, sigma in nm\), REFPROP's constant; Eq\. \(6\) with CODATA's k\_B gives 1\.38e\-4 more \(computed 2026\-09\-30\)\. optmat uses 0\.026692, the report's own check values and the WebBook's tables; the difference is far below every stated uncertainty\. F\_c\. For neon, krypton and xenon F\_c was adjusted so that the dilute\-gas viscosity at 25 C and 0\.1 MPa agrees with the reference values of Assael et al\. \(2018\) \(sections 6\.9\.1\-6\.9\.3\), which are therefore not an independent check\. For nitrous oxide F\_c = 1\. UNCERTAINTY \(expanded, coverage factor two, 'approximately a 95 % confidence interval', pdf p\. 14\)\: neon, 2 % in the supercritical region at atmospheric pressure \(section 6\.9\.1, pdf p\. 185\); krypton, 3 % in the gas phase at atmospheric pressure \(6\.9\.2, p\. 188\); xenon, 0\.7 % in the vapour phase \(6\.9\.3, p\. 191\); nitrous oxide, 5 % in the gas phase \(6\.11\.2, p\. 201\)\. The WebBook's pages state 3 %, 3 %, 1 % and 10 % for the same models; the report governs\. optmat takes each gas's equation\-of\-state temperatures within Eq\. \(7\)'s 0\.3 \< T\* \< 100\. THE WEBBOOK TABLES \(data/external/nist\_webbook, captured 2026\-09\-30\) give the models' viscosity at 0\.1 MPa, 200\-400 K\: they exceed the dilute values by 0\.013 % \(neon\), 0\.13 % \(krypton\), 0\.21 % \(xenon\) and 0\.21 % \(nitrous oxide\) at 298\.15 K, and by 0\.028 %, 0\.33 %, 0\.54 % and 0\.52 % at 200 K, the density term, falling with temperature \(tests/test\_transport\.py\)\. **Recorded bibliographic identity status:** VALIDATED. This concerns identification of the source; it does not establish the scientific correctness of its contents. Datasets -------- No datasets are recorded. Formulas -------- huber\_2018/eq6\_eq7\_Ne ~~~~~~~~~~~~~~~~~~~~~~~~ .. code-block:: text { "id": "eq6_eq7_Ne", "material": "Ne", "equation": "Eqs. (6)-(7), pdf p. 9; Tables 1-2, pdf pp. 262, 265", "printed": "eta* = 5 sqrt(m pi k_B T)/(16 pi sigma^2 Omega(2,2)) F_c; Omega(2,2) = 1.16145 T*^-0.14874 + 0.52487 exp(-0.77320 T*) + 2.16178 exp(-2.43787 T*)", "variable": "T* = k_B T/epsilon, 0.3 < T* < 100; eta* = 0.026692 sqrt(M T)/(sigma^2 Omega) F_c in uPa s, M in g/mol, sigma in nm", "range": "0.3 < T* < 100", "coefficients": { "prefactor": "0.026692", "molar_mass": "20.179", "epsilon_k": "45.58", "sigma_nm": "0.2707", "f_c": "0.989544" }, "check": "Table 7: 6.006075 uPa s at 40 K, reproduced to 6e-8." } huber\_2018/eq6\_eq7\_Kr ~~~~~~~~~~~~~~~~~~~~~~~~ .. code-block:: text { "id": "eq6_eq7_Kr", "material": "Kr", "equation": "Eqs. (6)-(7), pdf p. 9; Tables 1-2, pdf pp. 262, 265", "printed": "eta* = 5 sqrt(m pi k_B T)/(16 pi sigma^2 Omega(2,2)) F_c; Omega(2,2) = 1.16145 T*^-0.14874 + 0.52487 exp(-0.77320 T*) + 2.16178 exp(-2.43787 T*)", "variable": "T* = k_B T/epsilon, 0.3 < T* < 100; eta* = 0.026692 sqrt(M T)/(sigma^2 Omega) F_c in uPa s, M in g/mol, sigma in nm", "range": "0.3 < T* < 100", "coefficients": { "prefactor": "0.026692", "molar_mass": "83.798", "epsilon_k": "178.9", "sigma_nm": "0.3655", "f_c": "1.008291" }, "check": "Table 7: 16.32999 uPa s at 188.5 K, reproduced to 1.7e-7." } huber\_2018/eq6\_eq7\_Xe ~~~~~~~~~~~~~~~~~~~~~~~~ .. code-block:: text { "id": "eq6_eq7_Xe", "material": "Xe", "equation": "Eqs. (6)-(7), pdf p. 9; Tables 1-2, pdf pp. 262, 265", "printed": "eta* = 5 sqrt(m pi k_B T)/(16 pi sigma^2 Omega(2,2)) F_c; Omega(2,2) = 1.16145 T*^-0.14874 + 0.52487 exp(-0.77320 T*) + 2.16178 exp(-2.43787 T*)", "variable": "T* = k_B T/epsilon, 0.3 < T* < 100; eta* = 0.026692 sqrt(M T)/(sigma^2 Omega) F_c in uPa s, M in g/mol, sigma in nm", "range": "0.3 < T* < 100", "coefficients": { "prefactor": "0.026692", "molar_mass": "131.293", "epsilon_k": "260.91", "sigma_nm": "0.3929", "f_c": "1.0012" }, "check": "Table 7: 20.11099 uPa s at 260.8 K, reproduced to 2.4e-7." } huber\_2018/eq6\_eq7\_N2O ~~~~~~~~~~~~~~~~~~~~~~~~~ .. code-block:: text { "id": "eq6_eq7_N2O", "material": "N2O", "equation": "Eqs. (6)-(7), pdf p. 9; Tables 1-2, pdf pp. 262, 265", "printed": "eta* = 5 sqrt(m pi k_B T)/(16 pi sigma^2 Omega(2,2)) F_c; Omega(2,2) = 1.16145 T*^-0.14874 + 0.52487 exp(-0.77320 T*) + 2.16178 exp(-2.43787 T*)", "variable": "T* = k_B T/epsilon, 0.3 < T* < 100; eta* = 0.026692 sqrt(M T)/(sigma^2 Omega) F_c in uPa s, M in g/mol, sigma in nm", "range": "0.3 < T* < 100", "coefficients": { "prefactor": "0.026692", "molar_mass": "44.0128", "epsilon_k": "232.4", "sigma_nm": "0.3828", "f_c": "1" }, "check": "Table 7: 13.86694 uPa s at 278.6 K, reproduced to 2e-8." } Corrections ----------- No dataset errata are recorded in this source record. Formula corrections, where recorded, appear with their formulas above. Curation notes may also discuss corrections or unresolved interpretation. Consult the :doc:`review register ` for the checks and decisions.