- InChI
- InChI=1S/C2H6O/c1-3-2/h1-2H3
- InChI Key
- LCGLNKUTAGEVQW-UHFFFAOYSA-N
- Formula
- C2H6O
- SMILES
- COC
- Molecular Weight1
- 46.07
- CAS
- 115-10-6
- Other Names
-
- (CH3)2O
- DIMETHYL OXIDE
- DME
- Demeon D
- Dymel
- Dymel A
- Ether, dimethyl
- Ether, methyl
- METHYL ETHER
- Methane, 1,1'-oxybis-
- Methane, oxybis-
- Methoxymethane
- OXYBIS-METHANE
- Oxybismethane
- UN 1033
- Wood ether
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°gas : Standard gas enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρg : Gas Density (kg/m3).
- ρl : Liquid Density (kg/m3).
- ρm,g : Gas Amount Density (mol/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- B2 : 2nd virial coefficient (m3/mol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2000 | KDB | |
| PAff | 792.00 | kJ/mol | NIST |
| Tig | 623.15 | K | KDB |
| BasG | 764.50 | kJ/mol | NIST |
| ΔcH°gas | -1460.40 ± 0.46 | kJ/mol | NIST |
| μ | 1.30 | debye | KDB |
| LFL | 2.00 | % in Air | KDB |
| UFL | 50.00 | % in Air | KDB |
| ΔfG° | -113.00 | kJ/mol | KDB |
| ΔfH°gas | [-184.20; -184.10] | kJ/mol |
|
| ΔfH°gas | -184.20 | kJ/mol | KDB |
| ΔfH°gas | -184.10 ± 0.50 | kJ/mol | NIST |
| ΔfusH° | 2.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [18.50; 19.30] | kJ/mol |
|
| ΔvapH° | 19.30 | kJ/mol | NIST |
| ΔvapH° | 18.50 | kJ/mol | NIST |
| IE | [9.80; 11.94] | eV |
|
| IE | 10.03 ± 0.03 | eV | NIST |
| IE | 10.03 ± 0.03 | eV | NIST |
| IE | 9.95 ± 0.07 | eV | NIST |
| IE | 10.04 | eV | NIST |
| IE | 9.80 ± 0.10 | eV | NIST |
| IE | 9.80 | eV | NIST |
| IE | 10.01 ± 0.01 | eV | NIST |
| IE | 9.94 ± 0.01 | eV | NIST |
| IE | 10.10 ± 0.20 | eV | NIST |
| IE | 9.94 | eV | NIST |
| IE | 9.96 ± 0.05 | eV | NIST |
| IE | 10.00 ± 0.02 | eV | NIST |
| IE | 10.00 | eV | NIST |
| IE | 10.10 | eV | NIST |
| IE | Outlier 11.94 | eV | NIST |
| IE | 10.00 ± 0.20 | eV | NIST |
| IE | 10.10 | eV | NIST |
| IE | 10.03 | eV | NIST |
| IE | 9.98 | eV | NIST |
| IE | 10.05 | eV | NIST |
| IE | 10.04 | eV | NIST |
| IE | 10.04 | eV | NIST |
| log10WS | 0.25 | Crippen Calculated Property | |
| logPoct/wat | 0.263 | Crippen Calculated Property | |
| McVol | 44.910 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 4 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [5264.00; 5800.00] | kPa |
|
| Pc | 5370.00 | kPa | KDB |
| Pc | 5340.50 | kPa | Experim... |
| Pc | 5356.00 | kPa | Measure... |
| Pc | 5267.00 | kPa | Critica... |
| Pc | 5264.00 ± 15.00 | kPa | NIST |
| Pc | 5359.00 ± 50.66 | kPa | NIST |
| Pc | 5330.00 ± 60.79 | kPa | NIST |
| Pc | 5400.00 ± 101.32 | kPa | NIST |
| Pc | 5269.00 ± 40.53 | kPa | NIST |
| Pc | 5400.00 ± 101.32 | kPa | NIST |
| Pc | 5400.00 ± 151.99 | kPa | NIST |
| Pc | Outlier 5800.00 ± 405.30 | kPa | NIST |
| ρc | [225.50; 271.39] | kg/m3 |
|
| ρc | 246.51 ± 19.81 | kg/m3 | NIST |
| ρc | 225.50 ± 29.94 | kg/m3 | NIST |
| ρc | 271.39 ± 3.22 | kg/m3 | NIST |
| Inp | [323.00; 350.00] |
|
|
| Inp | 323.00 | NIST | |
| Inp | 325.00 | NIST | |
| Inp | 324.00 | NIST | |
| Inp | 331.00 | NIST | |
| Inp | 323.00 | NIST | |
| Inp | 327.00 | NIST | |
| Inp | Outlier 350.00 | NIST | |
| Inp | 328.00 | NIST | |
| Inp | 327.00 | NIST | |
| Inp | 328.00 | NIST | |
| Inp | 323.00 | NIST | |
| I | [478.00; 524.00] |
|
|
| I | 478.00 | NIST | |
| I | 481.00 | NIST | |
| I | 524.00 | NIST | |
| I | 524.00 | NIST | |
| S°liquid | 146.57 | J/mol×K | NIST |
| Tboil | [248.20; 249.50] | K |
|
| Tboil | 248.30 | K | KDB |
| Tboil | 248.20 | K | NIST |
| Tboil | 248.30 | K | NIST |
| Tboil | 248.45 | K | NIST |
| Tboil | 248.25 ± 1.00 | K | NIST |
| Tboil | 249.20 ± 0.40 | K | NIST |
| Tboil | 249.50 ± 0.60 | K | NIST |
| Tc | [399.40; 402.80] | K |
|
| Tc | 400.00 | K | KDB |
| Tc | 399.40 ± 0.15 | K | NIST |
| Tc | 400.33 ± 1.00 | K | NIST |
| Tc | 400.10 ± 0.40 | K | NIST |
| Tc | 400.10 ± 0.40 | K | NIST |
| Tc | 399.70 ± 0.40 | K | NIST |
| Tc | 399.40 ± 0.40 | K | NIST |
| Tc | 400.05 ± 0.30 | K | NIST |
| Tc | 402.80 ± 3.00 | K | NIST |
| Tc | 400.30 ± 0.40 | K | NIST |
| Tc | 400.00 ± 2.00 | K | NIST |
| Tc | 402.80 ± 3.00 | K | NIST |
| Tc | 402.80 ± 3.00 | K | NIST |
| Tfus | [131.60; 135.20] | K |
|
| Tfus | 131.60 | K | KDB |
| Tfus | 131.65 | K | NIST |
| Tfus | 135.20 ± 2.00 | K | NIST |
| Ttriple | [131.64; 131.66] | K |
|
| Ttriple | 131.64 ± 0.05 | K | NIST |
| Ttriple | 131.66 ± 0.06 | K | NIST |
| Vc | [0.164; 0.190] | m3/kmol |
|
| Vc | 0.190 | m3/kmol | KDB |
| Vc | 0.164 ± 0.003 | m3/kmol | NIST |
| Zc | 0.3067830 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [62.01; 75.14] | J/mol×K | [272.20; 370.42] |
|
| Cp,gas | 62.01 | J/mol×K | 272.20 | NIST |
| Cp,gas | 65.90 | J/mol×K | 300.76 | NIST |
| Cp,gas | 70.33 | J/mol×K | 333.25 | NIST |
| Cp,gas | 75.14 | J/mol×K | 370.42 | NIST |
| Cp,liquid | 102.30 | J/mol×K | 240.00 | NIST |
| η | [0.0000626; 0.0002217] | Pa×s | [243.15; 373.13] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-5 1.00e-4 1.50e-4 2.00e-4 250 300 350 | ||||
| η | 0.0002217 | Pa×s | 243.15 | Experim... |
| η | 0.0002097 | Pa×s | 248.16 | Experim... |
| η | 0.0001989 | Pa×s | 253.15 | Experim... |
| η | 0.0001889 | Pa×s | 258.14 | Experim... |
| η | 0.0001796 | Pa×s | 263.15 | Experim... |
| η | 0.0001709 | Pa×s | 268.14 | Experim... |
| η | 0.0001627 | Pa×s | 273.14 | Experim... |
| η | 0.0001552 | Pa×s | 278.13 | Experim... |
| η | 0.0001479 | Pa×s | 283.14 | Experim... |
| η | 0.0001414 | Pa×s | 288.14 | Experim... |
| η | 0.0001351 | Pa×s | 293.14 | Experim... |
| η | 0.0001290 | Pa×s | 298.14 | Experim... |
| η | 0.0001240 | Pa×s | 303.14 | Experim... |
| η | 0.0001181 | Pa×s | 308.14 | Experim... |
| η | 0.0001129 | Pa×s | 313.14 | Experim... |
| η | 0.0001080 | Pa×s | 318.12 | Experim... |
| η | 0.0001031 | Pa×s | 323.12 | Experim... |
| η | 0.0000986 | Pa×s | 328.12 | Experim... |
| η | 0.0000942 | Pa×s | 333.13 | Experim... |
| η | 0.0000898 | Pa×s | 338.13 | Experim... |
| η | 0.0000857 | Pa×s | 343.13 | Experim... |
| η | 0.0000817 | Pa×s | 348.13 | Experim... |
| η | 0.0000778 | Pa×s | 353.12 | Experim... |
| η | 0.0000739 | Pa×s | 358.13 | Experim... |
| η | 0.0000701 | Pa×s | 363.13 | Experim... |
| η | 0.0000664 | Pa×s | 368.13 | Experim... |
| η | 0.0000626 | Pa×s | 373.13 | Experim... |
| ΔfusH | [4.94; 4.94] | kJ/mol | [131.66; 131.70] |
|
| ΔfusH | 4.94 | kJ/mol | 131.66 | NIST |
| ΔfusH | 4.94 | kJ/mol | 131.70 | NIST |
| ΔfusH | 4.94 | kJ/mol | 131.70 | NIST |
| ΔvapH | [21.10; 22.80] | kJ/mol | [209.50; 374.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 21 21.5 22 22.5 250 300 350 | ||||
| ΔvapH | 21.40 | kJ/mol | 209.50 | NIST |
| ΔvapH | 22.80 | kJ/mol | 214.50 | NIST |
| ΔvapH | 22.70 | kJ/mol | 221.50 | NIST |
| ΔvapH | 22.60 | kJ/mol | 224.00 | NIST |
| ΔvapH | 21.50 ± 0.10 | kJ/mol | 248.00 | NIST |
| ΔvapH | 21.51 | kJ/mol | 248.30 | NIST |
| ΔvapH | 21.51 | kJ/mol | 248.34 | NIST |
| ΔvapH | 21.51 | kJ/mol | 249.20 | KDB |
| ΔvapH | 22.20 | kJ/mol | 272.00 | NIST |
| ΔvapH | 21.20 | kJ/mol | 326.50 | NIST |
| ΔvapH | 21.10 | kJ/mol | 374.50 | NIST |
| ν | [0.0000002; 0.0000003] | m2/s | [227.22; 342.45] |
|
|
T(K) Kinematic viscosity (m2/s) 1.50e-7 2.00e-7 2.50e-7 3.00e-7 3.50e-7 250 300 | ||||
| ν | 0.0000003 | m2/s | 227.22 | Viscosi... |
| ν | 0.0000003 | m2/s | 232.28 | Viscosi... |
| ν | 0.0000003 | m2/s | 237.47 | Viscosi... |
| ν | 0.0000003 | m2/s | 243.15 | Viscosi... |
| ν | 0.0000003 | m2/s | 248.30 | Viscosi... |
| ν | 0.0000003 | m2/s | 253.14 | Viscosi... |
| ν | 0.0000002 | m2/s | 258.15 | Viscosi... |
| ν | 0.0000002 | m2/s | 263.14 | Viscosi... |
| ν | 0.0000002 | m2/s | 268.15 | Viscosi... |
| ν | 0.0000002 | m2/s | 273.16 | Viscosi... |
| ν | 0.0000002 | m2/s | 278.16 | Viscosi... |
| ν | 0.0000002 | m2/s | 283.15 | Viscosi... |
| ν | 0.0000002 | m2/s | 288.15 | Viscosi... |
| ν | 0.0000002 | m2/s | 293.14 | Viscosi... |
| ν | 0.0000002 | m2/s | 298.16 | Viscosi... |
| ν | 0.0000002 | m2/s | 303.16 | Viscosi... |
| ν | 0.0000002 | m2/s | 308.15 | Viscosi... |
| ν | 0.0000002 | m2/s | 312.53 | Viscosi... |
| ν | 0.0000002 | m2/s | 317.52 | Viscosi... |
| ν | 0.0000002 | m2/s | 322.50 | Viscosi... |
| ν | 0.0000002 | m2/s | 327.50 | Viscosi... |
| ν | 0.0000002 | m2/s | 332.49 | Viscosi... |
| ν | 0.0000002 | m2/s | 337.47 | Viscosi... |
| ν | 0.0000002 | m2/s | 342.45 | Viscosi... |
| Pvap | [16.46; 5355.80] | kPa | [213.08; 400.38] |
|
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 250 300 350 400 | ||||
| Pvap | 16.46 | kPa | 213.08 | Vapor P... |
| Pvap | 22.24 | kPa | 218.11 | Vapor P... |
| Pvap | 22.30 | kPa | 219.15 | Saturat... |
| Pvap | 25.20 | kPa | 221.13 | Saturat... |
| Pvap | 28.30 | kPa | 223.11 | Saturat... |
| Pvap | 29.61 | kPa | 223.15 | Vapor P... |
| Pvap | 31.50 | kPa | 224.88 | Saturat... |
| Pvap | 35.40 | kPa | 226.88 | Saturat... |
| Pvap | 38.64 | kPa | 228.06 | Vapor P... |
| Pvap | 39.50 | kPa | 228.85 | Saturat... |
| Pvap | 43.90 | kPa | 230.86 | Saturat... |
| Pvap | 48.70 | kPa | 232.86 | Saturat... |
| Pvap | 49.96 | kPa | 233.09 | Vapor P... |
| Pvap | 54.61 | kPa | 233.13 | Vapor P... |
| Pvap | 54.10 | kPa | 234.85 | Saturat... |
| Pvap | 59.80 | kPa | 236.85 | Saturat... |
| Pvap | 63.84 | kPa | 238.11 | Vapor P... |
| Pvap | 68.49 | kPa | 238.13 | Vapor P... |
| Pvap | 66.30 | kPa | 239.14 | Saturat... |
| Pvap | 73.20 | kPa | 241.14 | Saturat... |
| Pvap | 80.36 | kPa | 243.07 | Vapor P... |
| Pvap | 85.57 | kPa | 243.16 | Vapor P... |
| Pvap | 84.00 | kPa | 244.14 | Saturat... |
| Pvap | 96.10 | kPa | 247.13 | Saturat... |
| Pvap | 100.43 | kPa | 248.12 | Vapor P... |
| Pvap | 105.59 | kPa | 248.15 | Vapor P... |
| Pvap | 104.90 | kPa | 249.13 | Saturat... |
| Pvap | 114.30 | kPa | 251.14 | Saturat... |
| Pvap | 125.00 | kPa | 253.05 | Vapor-L... |
| Pvap | 124.09 | kPa | 253.12 | Vapor P... |
| Pvap | 129.42 | kPa | 253.15 | Vapor P... |
| Pvap | 135.10 | kPa | 255.13 | Saturat... |
| Pvap | 146.60 | kPa | 257.12 | Saturat... |
| Pvap | 152.40 | kPa | 258.13 | Vapor P... |
| Pvap | 152.90 | kPa | 258.15 | Isother... |
| Pvap | 157.53 | kPa | 258.16 | Vapor P... |
| Pvap | 159.00 | kPa | 259.14 | Saturat... |
| Pvap | 171.80 | kPa | 261.13 | Saturat... |
| Pvap | 185.60 | kPa | 263.13 | Saturat... |
| Pvap | 184.96 | kPa | 263.13 | Vapor P... |
| Pvap | 190.44 | kPa | 263.16 | Vapor P... |
| Pvap | 199.80 | kPa | 265.13 | Saturat... |
| Pvap | 215.50 | kPa | 267.13 | Saturat... |
| Pvap | 222.70 | kPa | 268.13 | Vapor P... |
| Pvap | 228.48 | kPa | 268.16 | Vapor P... |
| Pvap | 231.80 | kPa | 269.13 | Saturat... |
| Pvap | 248.90 | kPa | 271.13 | Saturat... |
| Pvap | 266.80 | kPa | 273.13 | Saturat... |
| Pvap | 266.80 | kPa | 273.15 | Isother... |
| Pvap | 272.17 | kPa | 273.15 | Vapor P... |
| Pvap | 266.50 | kPa | 273.17 | Vapor P... |
| Pvap | 285.10 | kPa | 275.04 | Saturat... |
| Pvap | 305.00 | kPa | 277.02 | Saturat... |
| Pvap | 321.87 | kPa | 278.14 | Vapor P... |
| Pvap | 316.12 | kPa | 278.17 | Vapor P... |
| Pvap | 317.60 | kPa | 278.25 | Vapour ... |
| Pvap | 326.40 | kPa | 279.02 | Saturat... |
| Pvap | 348.80 | kPa | 281.02 | Saturat... |
| Pvap | 372.30 | kPa | 283.02 | Saturat... |
| Pvap | 372.00 | kPa | 283.15 | Isother... |
| Pvap | 372.90 | kPa | 283.16 | Vapor P... |
| Pvap | 378.66 | kPa | 283.16 | Vapor P... |
| Pvap | 373.60 | kPa | 283.20 | Vapour ... |
| Pvap | 397.00 | kPa | 285.01 | Saturat... |
| Pvap | 422.80 | kPa | 287.00 | Saturat... |
| Pvap | 436.69 | kPa | 288.13 | Vapor P... |
| Pvap | 443.57 | kPa | 288.17 | Vapor P... |
| Pvap | 437.40 | kPa | 288.19 | Vapour ... |
| Pvap | 449.80 | kPa | 288.99 | Saturat... |
| Pvap | 478.40 | kPa | 290.99 | Saturat... |
| Pvap | 520.00 | kPa | 293.00 | Vapor-L... |
| Pvap | 508.90 | kPa | 293.08 | Saturat... |
| Pvap | 509.30 | kPa | 293.15 | Isother... |
| Pvap | 501.00 | kPa | 293.15 | Isother... |
| Pvap | 508.10 | kPa | 293.15 | Vapor-L... |
| Pvap | 515.53 | kPa | 293.16 | Vapor P... |
| Pvap | 509.01 | kPa | 293.17 | Vapor P... |
| Pvap | 509.40 | kPa | 293.20 | Vapour ... |
| Pvap | 540.00 | kPa | 295.07 | Saturat... |
| Pvap | 571.90 | kPa | 296.78 | Vapor-l... |
| Pvap | 573.00 | kPa | 297.07 | Saturat... |
| Pvap | 588.17 | kPa | 298.08 | Vapor P... |
| Pvap | 596.21 | kPa | 298.17 | Vapor P... |
| Pvap | 589.60 | kPa | 298.19 | Vapour ... |
| Pvap | 600.51 | kPa | 298.78 | Vapor P... |
| Pvap | 606.90 | kPa | 299.08 | Saturat... |
| Pvap | 643.10 | kPa | 301.11 | Saturat... |
| Pvap | 680.20 | kPa | 303.08 | Saturat... |
| Pvap | 687.00 | kPa | 303.15 | Isother... |
| Pvap | 679.68 | kPa | 303.15 | Vapor P... |
| Pvap | 687.37 | kPa | 303.16 | Vapor P... |
| Pvap | 679.20 | kPa | 303.18 | Vapour ... |
| Pvap | 678.10 | kPa | 303.19 | Vapour ... |
| Pvap | 690.20 | kPa | 303.46 | Vapor-l... |
| Pvap | 691.56 | kPa | 303.78 | Vapor P... |
| Pvap | 718.40 | kPa | 305.07 | Saturat... |
| Pvap | 726.26 | kPa | 305.16 | Vapor P... |
| Pvap | 758.80 | kPa | 307.07 | Saturat... |
| Pvap | 788.00 | kPa | 308.10 | Vapor-L... |
| Pvap | 778.92 | kPa | 308.13 | Vapor P... |
| Pvap | 785.20 | kPa | 308.13 | Vapor-L... |
| Pvap | 786.60 | kPa | 308.14 | Vapor L... |
| Pvap | 787.07 | kPa | 308.16 | Vapor P... |
| Pvap | 778.70 | kPa | 308.19 | Vapour ... |
| Pvap | 793.10 | kPa | 308.54 | Vapor-l... |
| Pvap | 800.70 | kPa | 309.06 | Saturat... |
| Pvap | 844.20 | kPa | 311.07 | Saturat... |
| Pvap | 875.30 | kPa | 312.26 | Vapor-l... |
| Pvap | 900.00 | kPa | 313.00 | Vapor-L... |
| Pvap | 889.50 | kPa | 313.06 | Saturat... |
| Pvap | 887.00 | kPa | 313.15 | (Vapour... |
| Pvap | 898.00 | kPa | 313.15 | Isother... |
| Pvap | 884.00 | kPa | 313.15 | Vapor l... |
| Pvap | 897.59 | kPa | 313.16 | Vapor P... |
| Pvap | 889.98 | kPa | 313.17 | Vapor P... |
| Pvap | 888.80 | kPa | 313.20 | Vapour ... |
| Pvap | 936.60 | kPa | 315.06 | Saturat... |
| Pvap | 968.55 | kPa | 316.15 | Vapor P... |
| Pvap | 985.30 | kPa | 317.04 | Saturat... |
| Pvap | 993.30 | kPa | 317.17 | Vapor-l... |
| Pvap | 1018.91 | kPa | 318.16 | Vapor P... |
| Pvap | 1011.55 | kPa | 318.16 | Vapor P... |
| Pvap | 1009.50 | kPa | 318.19 | Vapour ... |
| Pvap | 1036.00 | kPa | 319.03 | Saturat... |
| Pvap | 1088.70 | kPa | 321.03 | Saturat... |
| Pvap | 1122.00 | kPa | 322.08 | Vapor-l... |
| Pvap | 1143.30 | kPa | 323.02 | Saturat... |
| Pvap | 1152.35 | kPa | 323.15 | Vapor P... |
| Pvap | 1116.20 | kPa | 323.15 | Isother... |
| Pvap | 1147.00 | kPa | 323.15 | (Vapour... |
| Pvap | 1141.00 | kPa | 323.15 | Vapor l... |
| Pvap | 1144.73 | kPa | 323.17 | Vapor P... |
| Pvap | 1144.50 | kPa | 323.28 | Vapour ... |
| Pvap | 1146.20 | kPa | 323.37 | Vapour ... |
| Pvap | 1200.60 | kPa | 325.02 | Saturat... |
| Pvap | 1265.60 | kPa | 327.08 | Vapor-l... |
| Pvap | 1262.30 | kPa | 327.13 | Saturat... |
| Pvap | 1298.23 | kPa | 328.15 | Vapor P... |
| Pvap | 1290.23 | kPa | 328.16 | Vapor P... |
| Pvap | 1289.20 | kPa | 328.25 | Vapour ... |
| Pvap | 1319.90 | kPa | 329.02 | Saturat... |
| Pvap | 1385.30 | kPa | 331.11 | Saturat... |
| Pvap | 1423.50 | kPa | 332.09 | Vapor-l... |
| Pvap | 1450.60 | kPa | 333.11 | Saturat... |
| Pvap | 1451.00 | kPa | 333.15 | (Vapour... |
| Pvap | 1451.00 | kPa | 333.15 | Vapor l... |
| Pvap | 1457.50 | kPa | 333.16 | Vapor P... |
| Pvap | 1457.76 | kPa | 333.16 | Vapor P... |
| Pvap | 1449.22 | kPa | 333.17 | Vapor P... |
| Pvap | 1447.20 | kPa | 333.23 | Vapour ... |
| Pvap | 1518.80 | kPa | 335.11 | Saturat... |
| Pvap | 1540.00 | kPa | 335.63 | Vapor L... |
| Pvap | 1539.60 | kPa | 335.65 | Vapor-L... |
| Pvap | 1572.20 | kPa | 336.63 | Vapor L... |
| Pvap | 1576.50 | kPa | 336.67 | Vapor-l... |
| Pvap | 1572.20 | kPa | 336.70 | Vapor L... |
| Pvap | 1591.10 | kPa | 337.00 | Vapor-l... |
| Pvap | 1588.40 | kPa | 337.10 | Saturat... |
| Pvap | 1631.01 | kPa | 338.15 | Vapor P... |
| Pvap | 1621.53 | kPa | 338.17 | Vapor P... |
| Pvap | 1619.90 | kPa | 338.23 | Vapour ... |
| Pvap | 1660.30 | kPa | 339.10 | Saturat... |
| Pvap | 1733.30 | kPa | 341.08 | Saturat... |
| Pvap | 1773.80 | kPa | 341.97 | Vapor-l... |
| Pvap | 1811.30 | kPa | 343.09 | Saturat... |
| Pvap | 1818.80 | kPa | 343.15 | Vapor P... |
| Pvap | 1817.00 | kPa | 343.15 | Vapor l... |
| Pvap | 1817.00 | kPa | 343.15 | (Vapour... |
| Pvap | 1809.11 | kPa | 343.16 | Vapor P... |
| Pvap | 1805.30 | kPa | 343.18 | Vapour ... |
| Pvap | 1814.40 | kPa | 343.41 | Vapour ... |
| Pvap | 1891.20 | kPa | 345.09 | Saturat... |
| Pvap | 1976.20 | kPa | 347.00 | Vapor-l... |
| Pvap | 1972.80 | kPa | 347.08 | Saturat... |
| Pvap | 1976.80 | kPa | 347.42 | Vapour ... |
| Pvap | 2022.45 | kPa | 348.15 | Vapor P... |
| Pvap | 2012.44 | kPa | 348.16 | Vapor P... |
| Pvap | 2007.30 | kPa | 348.17 | Vapour ... |
| Pvap | 2057.40 | kPa | 349.08 | Saturat... |
| Pvap | 2144.30 | kPa | 351.07 | Saturat... |
| Pvap | 2149.60 | kPa | 351.44 | Vapour ... |
| Pvap | 2187.40 | kPa | 351.89 | Vapor-l... |
| Pvap | 2240.00 | kPa | 353.00 | Vapor-L... |
| Pvap | 2232.70 | kPa | 353.05 | Saturat... |
| Pvap | 2224.50 | kPa | 353.10 | Vapour ... |
| Pvap | 2242.74 | kPa | 353.15 | Vapor P... |
| Pvap | 2251.00 | kPa | 353.15 | (Vapour... |
| Pvap | 2245.00 | kPa | 353.15 | Vapor l... |
| Pvap | 2243.07 | kPa | 353.16 | Vapor P... |
| Pvap | 2232.34 | kPa | 353.16 | Vapor P... |
| Pvap | 2240.00 | kPa | 353.45 | Vapour ... |
| Pvap | 2326.00 | kPa | 355.05 | Saturat... |
| Pvap | 2315.60 | kPa | 355.08 | Vapour ... |
| Pvap | 2333.30 | kPa | 355.46 | Vapour ... |
| Pvap | 2422.20 | kPa | 356.91 | Vapor-l... |
| Pvap | 2421.90 | kPa | 357.05 | Saturat... |
| Pvap | 2429.50 | kPa | 357.49 | Vapour ... |
| Pvap | 2479.92 | kPa | 358.14 | Vapor P... |
| Pvap | 2468.87 | kPa | 358.16 | Vapor P... |
| Pvap | 2520.30 | kPa | 359.05 | Saturat... |
| Pvap | 2528.50 | kPa | 359.49 | Vapour ... |
| Pvap | 2579.10 | kPa | 360.52 | Vapour ... |
| Pvap | 2621.50 | kPa | 361.04 | Saturat... |
| Pvap | 2675.20 | kPa | 361.94 | Vapor-l... |
| Pvap | 2735.67 | kPa | 363.15 | Vapor P... |
| Pvap | 2735.00 | kPa | 363.15 | Vapor l... |
| Pvap | 2738.00 | kPa | 363.15 | (Vapour... |
| Pvap | 2723.27 | kPa | 363.16 | Vapor P... |
| Pvap | 2946.30 | kPa | 366.96 | Vapor-l... |
| Pvap | 2996.38 | kPa | 368.14 | Vapor P... |
| Pvap | 3010.81 | kPa | 368.16 | Vapor P... |
| Pvap | 3230.30 | kPa | 371.84 | Vapor-l... |
| Pvap | 3260.00 | kPa | 373.00 | Vapor-L... |
| Pvap | 3291.17 | kPa | 373.14 | Vapor P... |
| Pvap | 3305.67 | kPa | 373.15 | Vapor P... |
| Pvap | 3546.40 | kPa | 376.91 | Vapor-l... |
| Pvap | 3622.60 | kPa | 378.15 | Vapor P... |
| Pvap | 3608.63 | kPa | 378.15 | Vapor P... |
| Pvap | 3739.00 | kPa | 379.82 | Vapor-l... |
| Pvap | 3950.30 | kPa | 382.88 | Vapor-l... |
| Pvap | 3962.25 | kPa | 383.14 | Vapor P... |
| Pvap | 3948.62 | kPa | 383.15 | Vapor P... |
| Pvap | 4161.90 | kPa | 385.83 | Vapor-l... |
| Pvap | 4309.60 | kPa | 387.81 | Vapor-l... |
| Pvap | 4331.48 | kPa | 388.15 | Vapor P... |
| Pvap | 4313.91 | kPa | 388.16 | Vapor P... |
| Pvap | 4463.70 | kPa | 389.81 | Vapor-l... |
| Pvap | 4625.60 | kPa | 391.86 | Vapor-l... |
| Pvap | 4725.02 | kPa | 393.16 | Vapor P... |
| Pvap | 4706.18 | kPa | 393.16 | Vapor P... |
| Pvap | 4783.00 | kPa | 393.81 | Vapor-l... |
| Pvap | 4943.60 | kPa | 395.74 | Vapor-l... |
| Pvap | 5146.82 | kPa | 398.16 | Vapor P... |
| Pvap | 5355.80 | kPa | 400.38 | Vapor P... |
| ρl | 667.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | 37.49 | J/mol×K | 131.66 | NIST |
| γ | [6.14e-04; 0.02] | N/m | [213.12; 390.00] |
|
|
T(K) Surface Tension (N/m) 0 5.00e-3 0.01 0.02 0.02 0.03 250 300 350 | ||||
| γ | 0.02 | N/m | 213.12 | Surface... |
| γ | 0.02 | N/m | 214.00 | Capilla... |
| γ | 0.02 | N/m | 220.00 | Capilla... |
| γ | 0.02 | N/m | 223.11 | Surface... |
| γ | 0.02 | N/m | 225.00 | Capilla... |
| γ | 0.02 | N/m | 228.19 | Surface... |
| γ | 0.02 | N/m | 230.00 | Capilla... |
| γ | 0.02 | N/m | 233.20 | KDB |
| γ | 0.02 | N/m | 233.31 | Surface... |
| γ | 0.02 | N/m | 235.00 | Capilla... |
| γ | 0.02 | N/m | 238.15 | Surface... |
| γ | 0.02 | N/m | 240.00 | Capilla... |
| γ | 0.02 | N/m | 243.12 | Surface... |
| γ | 0.02 | N/m | 245.00 | Capilla... |
| γ | 0.02 | N/m | 248.12 | Surface... |
| γ | 0.02 | N/m | 250.00 | Capilla... |
| γ | 0.02 | N/m | 253.09 | Surface... |
| γ | 0.02 | N/m | 255.00 | Capilla... |
| γ | 0.02 | N/m | 258.11 | Surface... |
| γ | 0.02 | N/m | 260.00 | Capilla... |
| γ | 0.02 | N/m | 263.12 | Surface... |
| γ | 0.02 | N/m | 265.00 | Capilla... |
| γ | 0.02 | N/m | 268.08 | Surface... |
| γ | 0.02 | N/m | 270.00 | Capilla... |
| γ | 0.02 | N/m | 273.08 | Surface... |
| γ | 0.02 | N/m | 275.00 | Capilla... |
| γ | 0.01 | N/m | 278.06 | Surface... |
| γ | 0.01 | N/m | 278.16 | Surface... |
| γ | 0.01 | N/m | 280.00 | Capilla... |
| γ | 0.01 | N/m | 283.07 | Surface... |
| γ | 0.01 | N/m | 283.21 | Surface... |
| γ | 0.01 | N/m | 285.00 | Capilla... |
| γ | 0.01 | N/m | 288.04 | Surface... |
| γ | 0.01 | N/m | 288.17 | Surface... |
| γ | 0.01 | N/m | 290.00 | Capilla... |
| γ | 0.01 | N/m | 293.09 | Surface... |
| γ | 0.01 | N/m | 293.15 | Surface... |
| γ | 0.01 | N/m | 295.00 | Capilla... |
| γ | 0.01 | N/m | 298.08 | Surface... |
| γ | 0.01 | N/m | 298.10 | Surface... |
| γ | 0.01 | N/m | 300.00 | Capilla... |
| γ | 0.01 | N/m | 303.13 | Surface... |
| γ | 0.01 | N/m | 303.20 | Surface... |
| γ | 0.01 | N/m | 305.00 | Capilla... |
| γ | 0.01 | N/m | 308.12 | Surface... |
| γ | 0.01 | N/m | 313.12 | Surface... |
| γ | 0.01 | N/m | 315.00 | Capilla... |
| γ | 0.01 | N/m | 318.18 | Surface... |
| γ | 0.01 | N/m | 320.00 | Capilla... |
| γ | 0.01 | N/m | 323.18 | Surface... |
| γ | 0.01 | N/m | 325.00 | Capilla... |
| γ | 0.01 | N/m | 328.14 | Surface... |
| γ | 0.01 | N/m | 330.00 | Capilla... |
| γ | 0.01 | N/m | 333.14 | Surface... |
| γ | 0.01 | N/m | 335.00 | Capilla... |
| γ | 0.01 | N/m | 338.09 | Surface... |
| γ | 0.01 | N/m | 340.00 | Capilla... |
| γ | 0.01 | N/m | 343.13 | Surface... |
| γ | 0.01 | N/m | 345.00 | Capilla... |
| γ | 0.01 | N/m | 348.07 | Surface... |
| γ | 0.00 | N/m | 350.00 | Capilla... |
| γ | 0.00 | N/m | 353.11 | Surface... |
| γ | 0.00 | N/m | 355.00 | Capilla... |
| γ | 0.00 | N/m | 358.11 | Surface... |
| γ | 0.00 | N/m | 360.00 | Capilla... |
| γ | 0.00 | N/m | 363.10 | Surface... |
| γ | 0.00 | N/m | 365.00 | Capilla... |
| γ | 0.00 | N/m | 368.04 | Surface... |
| γ | 0.00 | N/m | 370.00 | Capilla... |
| γ | 0.00 | N/m | 375.00 | Capilla... |
| γ | 0.00 | N/m | 380.00 | Capilla... |
| γ | 0.00 | N/m | 385.00 | Capilla... |
| γ | 6.14e-04 | N/m | 390.00 | Capilla... |
| ΔvapS | 86.61 | J/mol×K | 248.34 | NIST |
| λ | [0.15; 0.18] | W/m×K | [229.67; 291.33] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.15 0.16 0.16 0.16 0.17 0.18 0.18 0.19 240 260 280 | ||||
| λ | 0.18 | W/m×K | 229.67 | Thermal... |
| λ | 0.18 | W/m×K | 244.98 | Thermal... |
| λ | 0.17 | W/m×K | 254.60 | Thermal... |
| λ | 0.16 | W/m×K | 271.55 | Thermal... |
| λ | 0.15 | W/m×K | 281.76 | Thermal... |
| λ | 0.15 | W/m×K | 291.33 | Thermal... |
| B2 | [-3.42e-04; -2.15e-04] | m3/mol | [328.05; 403.16] |
|
|
T(K) 2nd virial coefficient (m3/mol) -3.40e-4 -3.20e-4 -3.00e-4 -2.80e-4 -2.60e-4 -2.40e-4 -2.20e-4 340 360 380 400 | ||||
| B2 | -3.42e-04 | m3/mol | 328.05 | Gas pha... |
| B2 | -3.28e-04 | m3/mol | 333.04 | Gas pha... |
| B2 | -3.21e-04 | m3/mol | 338.04 | Gas pha... |
| B2 | -3.11e-04 | m3/mol | 343.05 | Gas pha... |
| B2 | -3.02e-04 | m3/mol | 348.03 | Gas pha... |
| B2 | -2.94e-04 | m3/mol | 353.03 | Gas pha... |
| B2 | -2.84e-04 | m3/mol | 358.02 | Gas pha... |
| B2 | -2.75e-04 | m3/mol | 363.02 | Gas pha... |
| B2 | -2.67e-04 | m3/mol | 368.02 | Gas pha... |
| B2 | -2.59e-04 | m3/mol | 373.02 | Gas pha... |
| B2 | -2.51e-04 | m3/mol | 378.01 | Gas pha... |
| B2 | -2.44e-04 | m3/mol | 383.00 | Gas pha... |
| B2 | -2.36e-04 | m3/mol | 388.16 | Gas pha... |
| B2 | -2.29e-04 | m3/mol | 393.16 | Gas pha... |
| B2 | -2.22e-04 | m3/mol | 398.16 | Gas pha... |
| B2 | -2.15e-04 | m3/mol | 403.16 | Gas pha... |
Datasets
- Molar heat capacity at constant pressure, J/K/mol (2)
- Viscosity, Pa*s (1)
- Mass density, kg/m3 (1)
- Mass density, kg/m3 (3)
- Amount density, mol/m3 (1)
- Thermal conductivity, W/m/K (1)
- Thermal conductivity, W/m/K (1)
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 305.15 | 1460.00 | 113.19 |
| 305.15 | 2030.00 | 112.82 |
| 305.15 | 2520.00 | 112.13 |
| 305.15 | 2930.00 | 112.36 |
| 305.15 | 3540.00 | 111.99 |
| 305.15 | 4060.00 | 111.53 |
| 305.15 | 4580.00 | 111.26 |
| 305.15 | 5020.00 | 111.02 |
| 310.15 | 1460.00 | 113.47 |
| 310.15 | 2030.00 | 112.91 |
| 310.15 | 2520.00 | 112.31 |
| 310.15 | 2930.00 | 112.45 |
| 310.15 | 3540.00 | 111.72 |
| 310.15 | 4060.00 | 111.21 |
| 310.15 | 4580.00 | 111.44 |
| 310.15 | 5020.00 | 111.30 |
| 315.15 | 1460.00 | 114.80 |
| 315.15 | 2030.00 | 114.11 |
| 315.15 | 2520.00 | 113.60 |
| 315.15 | 2930.00 | 113.47 |
| 315.15 | 3540.00 | 112.78 |
| 315.15 | 4060.00 | 112.13 |
| 315.15 | 4580.00 | 112.45 |
| 315.15 | 5020.00 | 112.22 |
| 320.15 | 1460.00 | 116.23 |
| 320.15 | 2030.00 | 115.45 |
| 320.15 | 2520.00 | 115.03 |
| 320.15 | 2930.00 | 114.89 |
| 320.15 | 3540.00 | 114.02 |
| 320.15 | 4060.00 | 113.37 |
| 320.15 | 4580.00 | 113.56 |
| 320.15 | 5020.00 | 113.28 |
| 325.15 | 1460.00 | 117.84 |
| 325.15 | 2030.00 | 116.92 |
| 325.15 | 2520.00 | 116.65 |
| 325.15 | 2930.00 | 116.05 |
| 325.15 | 3540.00 | 115.31 |
| 325.15 | 4060.00 | 114.57 |
| 325.15 | 4580.00 | 114.66 |
| 325.15 | 5020.00 | 114.30 |
| 330.15 | 2030.00 | 118.86 |
| 330.15 | 2520.00 | 118.49 |
| 330.15 | 2930.00 | 117.75 |
| 330.15 | 3540.00 | 117.01 |
| 330.15 | 4060.00 | 116.05 |
| 330.15 | 4580.00 | 116.05 |
| 330.15 | 5020.00 | 115.59 |
| 335.15 | 2030.00 | 121.34 |
| 335.15 | 2520.00 | 120.84 |
| 335.15 | 2930.00 | 120.15 |
| 335.15 | 3540.00 | 119.27 |
| 335.15 | 4060.00 | 118.03 |
| 335.15 | 4580.00 | 117.98 |
| 335.15 | 5020.00 | 117.38 |
| 340.15 | 2520.00 | 123.92 |
| 340.15 | 2930.00 | 123.09 |
| 340.15 | 3540.00 | 122.08 |
| 340.15 | 4060.00 | 120.65 |
| 340.15 | 4580.00 | 120.52 |
| 340.15 | 5020.00 | 119.82 |
| 345.15 | 2520.00 | 127.75 |
| 345.15 | 2930.00 | 126.55 |
| 345.15 | 3540.00 | 125.35 |
| 345.15 | 4060.00 | 123.92 |
| 345.15 | 4580.00 | 123.65 |
| 345.15 | 5020.00 | 122.86 |
| 350.15 | 2930.00 | 130.65 |
| 350.15 | 3540.00 | 129.13 |
| 350.15 | 4060.00 | 127.75 |
| 350.15 | 4580.00 | 127.19 |
| 350.15 | 5020.00 | 126.27 |
| 355.15 | 3540.00 | 133.46 |
| 355.15 | 4060.00 | 131.94 |
| 355.15 | 4580.00 | 131.06 |
| 355.15 | 5020.00 | 129.91 |
| 360.15 | 4060.00 | 136.82 |
| 360.15 | 4580.00 | 135.67 |
| 360.15 | 5020.00 | 134.15 |
| 365.15 | 4060.00 | 144.01 |
| 365.15 | 4580.00 | 142.31 |
| 365.15 | 5020.00 | 140.42 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 310.00 | 2000.00 | 123.92 |
| 310.00 | 3000.00 | 122.08 |
| 310.00 | 4000.00 | 121.62 |
| 310.00 | 5000.00 | 121.16 |
| 320.00 | 2000.00 | 127.61 |
| 320.00 | 3000.00 | 125.77 |
| 320.00 | 4000.00 | 124.85 |
| 320.00 | 5000.00 | 124.85 |
| 330.00 | 2000.00 | 131.30 |
| 330.00 | 3000.00 | 128.53 |
| 330.00 | 4000.00 | 128.07 |
| 330.00 | 5000.00 | 127.15 |
| 340.00 | 2000.00 | 137.74 |
| 340.00 | 3000.00 | 134.98 |
| 340.00 | 4000.00 | 132.22 |
| 340.00 | 5000.00 | 129.45 |
| 350.00 | 3000.00 | 140.51 |
| 350.00 | 4000.00 | 137.28 |
| 350.00 | 5000.00 | 132.68 |
| 360.00 | 3000.00 | 153.87 |
| 360.00 | 4000.00 | 145.12 |
| 360.00 | 5000.00 | 136.36 |
| Reference | ||
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Viscosity, Pa*s - Gas |
| 298.15 | 101.00 | 9.2200e-06 |
| 298.15 | 296.00 | 9.1800e-06 |
| 298.15 | 475.00 | 9.1000e-06 |
| 323.15 | 101.00 | 9.9700e-06 |
| 323.15 | 295.00 | 9.9600e-06 |
| 323.15 | 490.00 | 9.9300e-06 |
| 323.15 | 736.00 | 9.9500e-06 |
| 323.15 | 976.00 | 9.9400e-06 |
| 348.15 | 101.00 | 0.0000 |
| 348.15 | 305.00 | 0.0000 |
| 348.15 | 551.00 | 0.0000 |
| 348.15 | 1006.00 | 0.0000 |
| 348.15 | 1561.00 | 0.0000 |
| 348.15 | 1850.00 | 0.0000 |
| 373.15 | 101.00 | 0.0000 |
| 373.15 | 305.00 | 0.0000 |
| 373.15 | 500.00 | 0.0000 |
| 373.15 | 1028.00 | 0.0000 |
| 373.15 | 1940.00 | 0.0000 |
| 373.15 | 2505.00 | 0.0000 |
| 373.15 | 2875.00 | 0.0000 |
| 373.15 | 3049.00 | 0.0000 |
| 398.15 | 101.00 | 0.0000 |
| 398.15 | 300.00 | 0.0000 |
| 398.15 | 531.00 | 0.0000 |
| 398.15 | 992.00 | 0.0000 |
| 398.15 | 2085.00 | 0.0000 |
| 398.15 | 2985.00 | 0.0000 |
| 398.15 | 3965.00 | 0.0000 |
| 398.15 | 4480.00 | 0.0000 |
| 398.15 | 4620.00 | 0.0000 |
| 423.15 | 101.00 | 0.0000 |
| 423.15 | 310.00 | 0.0000 |
| 423.15 | 505.00 | 0.0000 |
| 423.15 | 985.00 | 0.0000 |
| 423.15 | 2022.00 | 0.0000 |
| 423.15 | 3004.00 | 0.0000 |
| 423.15 | 4015.00 | 0.0000 |
| 423.15 | 4495.00 | 0.0000 |
| 423.15 | 4912.00 | 0.0000 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Mass density, kg/m3 - Gas |
| 402.80 | 8580.00 | 451.0 |
| 411.60 | 10360.00 | 451.0 |
| 419.50 | 12150.00 | 451.0 |
| 425.40 | 13670.00 | 451.0 |
| 429.80 | 14600.00 | 451.0 |
| 432.60 | 15210.00 | 451.0 |
| 437.20 | 16200.00 | 451.0 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Fluid (supercritical or subcritical phases) | Temperature, K - Fluid (supercritical or subcritical phases) | Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
| 4100.00 | 288.50 | 684.0 |
| 5100.00 | 288.60 | 686.0 |
| 6100.00 | 288.80 | 688.0 |
| 7200.00 | 289.00 | 690.0 |
| 8200.00 | 289.10 | 691.0 |
| 9200.00 | 289.10 | 693.0 |
| 10000.00 | 289.30 | 694.0 |
| 15000.00 | 289.30 | 703.0 |
| 20000.00 | 289.30 | 711.0 |
| 25000.00 | 289.40 | 718.0 |
| 30000.00 | 289.50 | 725.0 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.84 | 1000.00 | 669.27 |
| 293.84 | 3000.00 | 673.21 |
| 293.84 | 5000.00 | 676.85 |
| 293.84 | 10000.00 | 685.08 |
| 293.84 | 15000.00 | 692.61 |
| 293.84 | 20000.00 | 699.44 |
| 293.84 | 25000.00 | 705.75 |
| 293.84 | 30000.00 | 711.53 |
| 293.84 | 35000.00 | 717.0 |
| 293.84 | 40000.00 | 722.21 |
| 293.84 | 50000.00 | 731.68 |
| 293.84 | 60000.00 | 740.35 |
| 293.84 | 70000.00 | 748.4 |
| 303.45 | 1000.00 | 653.54 |
| 303.45 | 3000.00 | 657.94 |
| 303.45 | 5000.00 | 662.06 |
| 303.45 | 10000.00 | 671.42 |
| 303.45 | 15000.00 | 679.73 |
| 303.45 | 20000.00 | 687.19 |
| 303.45 | 25000.00 | 694.14 |
| 303.45 | 30000.00 | 700.39 |
| 303.45 | 35000.00 | 706.33 |
| 303.45 | 40000.00 | 711.79 |
| 303.45 | 50000.00 | 721.98 |
| 303.45 | 60000.00 | 731.17 |
| 303.45 | 70000.00 | 739.59 |
| 313.18 | 3000.00 | 641.72 |
| 313.18 | 5000.00 | 646.5 |
| 313.18 | 10000.00 | 657.11 |
| 313.18 | 15000.00 | 666.38 |
| 313.18 | 20000.00 | 674.68 |
| 313.18 | 25000.00 | 682.06 |
| 313.18 | 30000.00 | 688.96 |
| 313.18 | 35000.00 | 695.3 |
| 313.18 | 40000.00 | 701.19 |
| 313.18 | 50000.00 | 711.96 |
| 313.18 | 60000.00 | 721.63 |
| 313.18 | 70000.00 | 730.55 |
| 323.00 | 3000.00 | 624.46 |
| 323.00 | 5000.00 | 630.01 |
| 323.00 | 10000.00 | 642.19 |
| 323.00 | 15000.00 | 652.54 |
| 323.00 | 20000.00 | 661.65 |
| 323.00 | 25000.00 | 669.81 |
| 323.00 | 30000.00 | 677.2 |
| 323.00 | 35000.00 | 684.06 |
| 323.00 | 40000.00 | 690.37 |
| 323.00 | 50000.00 | 701.9 |
| 323.00 | 60000.00 | 712.04 |
| 323.00 | 70000.00 | 721.44 |
| 332.83 | 3000.00 | 605.7 |
| 332.83 | 5000.00 | 612.33 |
| 332.83 | 10000.00 | 626.46 |
| 332.83 | 15000.00 | 638.17 |
| 332.83 | 20000.00 | 648.33 |
| 332.83 | 25000.00 | 657.3 |
| 332.83 | 30000.00 | 665.34 |
| 332.83 | 35000.00 | 672.7 |
| 332.83 | 40000.00 | 679.54 |
| 332.83 | 50000.00 | 691.67 |
| 332.83 | 60000.00 | 702.5 |
| 332.83 | 70000.00 | 712.29 |
| 343.01 | 3000.00 | 584.39 |
| 343.01 | 5000.00 | 592.63 |
| 343.01 | 10000.00 | 609.39 |
| 343.01 | 15000.00 | 622.87 |
| 343.01 | 20000.00 | 634.17 |
| 343.01 | 25000.00 | 644.06 |
| 343.01 | 30000.00 | 652.87 |
| 343.01 | 35000.00 | 660.84 |
| 343.01 | 40000.00 | 668.11 |
| 343.01 | 50000.00 | 681.15 |
| 343.01 | 60000.00 | 692.63 |
| 343.01 | 70000.00 | 702.89 |
| 353.00 | 3000.00 | 560.89 |
| 353.00 | 5000.00 | 571.39 |
| 353.00 | 10000.00 | 591.7 |
| 353.00 | 15000.00 | 607.19 |
| 353.00 | 20000.00 | 619.91 |
| 353.00 | 25000.00 | 630.86 |
| 353.00 | 30000.00 | 640.46 |
| 353.00 | 35000.00 | 649.09 |
| 353.00 | 40000.00 | 656.92 |
| 353.00 | 50000.00 | 670.8 |
| 353.00 | 60000.00 | 682.9 |
| 353.00 | 70000.00 | 693.76 |
| 362.91 | 5000.00 | 547.69 |
| 362.91 | 10000.00 | 572.99 |
| 362.91 | 15000.00 | 591.04 |
| 362.91 | 20000.00 | 605.41 |
| 362.91 | 25000.00 | 617.51 |
| 362.91 | 30000.00 | 627.99 |
| 362.91 | 35000.00 | 637.26 |
| 362.91 | 40000.00 | 645.67 |
| 362.91 | 50000.00 | 660.45 |
| 362.91 | 60000.00 | 673.27 |
| 362.91 | 70000.00 | 684.63 |
| 372.94 | 5000.00 | 519.39 |
| 372.94 | 10000.00 | 552.4 |
| 372.94 | 15000.00 | 573.78 |
| 372.94 | 20000.00 | 590.14 |
| 372.94 | 25000.00 | 603.55 |
| 372.94 | 30000.00 | 615.07 |
| 372.94 | 35000.00 | 625.15 |
| 372.94 | 40000.00 | 634.21 |
| 372.94 | 50000.00 | 649.98 |
| 372.94 | 60000.00 | 663.51 |
| 372.94 | 70000.00 | 675.48 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.14 | 2513.00 | 688.1 |
| 283.14 | 5003.00 | 692.0 |
| 283.14 | 9016.00 | 698.0 |
| 283.14 | 11009.00 | 700.8 |
| 283.14 | 18086.00 | 710.2 |
| 283.14 | 21845.00 | 714.6 |
| 283.14 | 32151.00 | 726.1 |
| 283.15 | 550.00 | 684.8 |
| 283.15 | 14790.00 | 705.9 |
| 283.15 | 25006.00 | 718.2 |
| 283.15 | 29056.00 | 722.8 |
| 283.16 | 35521.00 | 729.5 |
| 293.15 | 602.00 | 669.3 |
| 293.15 | 2506.00 | 672.9 |
| 293.15 | 5017.00 | 677.4 |
| 293.15 | 9039.00 | 684.2 |
| 293.15 | 11056.00 | 687.3 |
| 293.15 | 15028.00 | 693.2 |
| 293.15 | 18059.00 | 697.4 |
| 293.15 | 21007.00 | 701.4 |
| 293.15 | 25071.00 | 706.5 |
| 293.15 | 29096.00 | 711.3 |
| 293.15 | 32201.00 | 714.8 |
| 293.16 | 34680.00 | 717.5 |
| 303.15 | 804.00 | 653.8 |
| 303.15 | 9000.00 | 670.1 |
| 303.15 | 15007.00 | 680.1 |
| 303.15 | 19009.00 | 686.3 |
| 303.15 | 32101.00 | 703.7 |
| 303.16 | 2502.00 | 657.3 |
| 303.16 | 5002.00 | 662.5 |
| 303.16 | 11000.00 | 673.6 |
| 303.16 | 21216.00 | 689.5 |
| 303.16 | 25625.00 | 695.5 |
| 303.16 | 29118.00 | 700.0 |
| 303.16 | 35012.00 | 707.1 |
| 313.14 | 2207.00 | 639.8 |
| 313.14 | 29291.00 | 688.3 |
| 313.15 | 1003.00 | 636.8 |
| 313.15 | 5011.00 | 646.6 |
| 313.15 | 9070.00 | 655.3 |
| 313.15 | 11057.00 | 659.2 |
| 313.15 | 15041.00 | 666.5 |
| 313.15 | 19082.00 | 673.3 |
| 313.15 | 21159.00 | 676.6 |
| 313.15 | 25629.00 | 683.2 |
| 313.15 | 32000.00 | 692.0 |
| 313.15 | 35404.00 | 696.2 |
| 323.14 | 1750.00 | 620.4 |
| 323.14 | 4998.00 | 629.7 |
| 323.14 | 7033.00 | 634.9 |
| 323.14 | 10877.00 | 643.9 |
| 323.14 | 17659.00 | 657.5 |
| 323.14 | 23929.00 | 667.9 |
| 323.14 | 26052.00 | 671.4 |
| 323.14 | 32540.00 | 680.9 |
| 323.15 | 15253.00 | 652.9 |
| 323.15 | 20934.00 | 663.1 |
| 323.15 | 29643.00 | 676.8 |
| 323.15 | 35338.00 | 684.8 |
| 333.15 | 1545.00 | 600.4 |
| 333.15 | 3523.00 | 606.9 |
| 333.15 | 6504.00 | 616.3 |
| 333.15 | 9001.00 | 623.3 |
| 333.15 | 11059.00 | 628.5 |
| 333.15 | 14097.00 | 635.6 |
| 333.15 | 16998.00 | 642.0 |
| 333.15 | 20991.00 | 649.8 |
| 333.15 | 25004.00 | 657.1 |
| 333.15 | 29204.00 | 663.9 |
| 333.15 | 31963.00 | 668.2 |
| 333.15 | 35361.00 | 673.2 |
| 343.14 | 29042.00 | 651.5 |
| 343.15 | 3041.00 | 585.3 |
| 343.15 | 5002.00 | 593.1 |
| 343.15 | 8077.00 | 603.7 |
| 343.15 | 11043.00 | 612.6 |
| 343.15 | 12026.00 | 615.4 |
| 343.15 | 15026.00 | 623.1 |
| 343.15 | 18017.00 | 630.0 |
| 343.15 | 21209.00 | 636.9 |
| 343.15 | 25025.00 | 644.3 |
| 343.15 | 32018.00 | 656.5 |
| 343.16 | 35240.00 | 661.7 |
| 353.14 | 18102.00 | 615.2 |
| 353.14 | 22764.00 | 625.8 |
| 353.14 | 25005.00 | 630.8 |
| 353.15 | 7284.00 | 581.4 |
| 353.15 | 8162.00 | 584.8 |
| 353.15 | 9548.00 | 589.9 |
| 353.15 | 11065.00 | 594.9 |
| 353.15 | 15245.00 | 607.6 |
| 353.15 | 21002.00 | 622.2 |
| 353.15 | 29020.00 | 638.6 |
| 353.15 | 32599.00 | 645.3 |
| 353.15 | 35513.00 | 650.1 |
| Reference | ||
Amount density, mol/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Amount density, mol/m3 - Gas |
| 343.86 | 55.00 | 19.2 |
| 343.86 | 57.00 | 19.9 |
| 343.86 | 75.10 | 26.6 |
| 343.86 | 83.10 | 29.3 |
| 343.86 | 86.10 | 30.4 |
| 343.86 | 113.70 | 40.4 |
| 343.86 | 125.70 | 44.5 |
| 343.86 | 130.20 | 46.2 |
| 343.86 | 171.80 | 61.6 |
| 343.86 | 189.80 | 67.8 |
| 343.86 | 196.60 | 70.3 |
| 343.86 | 259.20 | 93.7 |
| 343.86 | 285.70 | 103.2 |
| 343.86 | 295.80 | 107.0 |
| 343.86 | 389.00 | 142.6 |
| 343.86 | 428.00 | 157.0 |
| 343.86 | 442.70 | 162.9 |
| 343.86 | 578.40 | 217.0 |
| 343.86 | 634.00 | 239.0 |
| 343.86 | 656.40 | 248.0 |
| 343.86 | 851.00 | 330.3 |
| 343.86 | 928.60 | 363.7 |
| 343.86 | 958.90 | 377.4 |
| 343.86 | 1225.60 | 502.7 |
| 343.86 | 1326.50 | 553.5 |
| 343.86 | 1365.40 | 574.4 |
| 343.86 | 1697.30 | 765.1 |
| 348.96 | 68.90 | 23.6 |
| 348.96 | 103.90 | 35.9 |
| 348.96 | 156.70 | 54.7 |
| 348.96 | 235.80 | 83.2 |
| 348.96 | 353.40 | 126.6 |
| 348.96 | 526.10 | 192.7 |
| 348.96 | 774.90 | 293.3 |
| 348.96 | 1121.10 | 446.4 |
| 348.96 | 1574.70 | 679.4 |
| 354.08 | 74.30 | 25.2 |
| 354.08 | 112.20 | 38.4 |
| 354.08 | 169.40 | 58.4 |
| 354.08 | 255.20 | 88.9 |
| 354.08 | 382.70 | 135.3 |
| 354.08 | 569.90 | 205.9 |
| 354.08 | 839.20 | 313.4 |
| 354.08 | 1212.90 | 477.0 |
| 354.08 | 1701.30 | 726.0 |
| 359.21 | 94.10 | 31.5 |
| 359.21 | 142.00 | 47.9 |
| 359.21 | 214.20 | 72.9 |
| 359.21 | 321.80 | 111.0 |
| 359.21 | 480.90 | 168.9 |
| 359.21 | 712.40 | 257.1 |
| 359.21 | 1040.80 | 391.3 |
| 359.21 | 1486.80 | 595.6 |
| 359.21 | 2045.90 | 906.5 |
| 364.35 | 103.80 | 34.6 |
| 364.35 | 157.10 | 52.6 |
| 364.35 | 237.30 | 80.1 |
| 364.35 | 357.20 | 121.9 |
| 364.35 | 534.50 | 185.5 |
| 364.35 | 790.30 | 282.3 |
| 364.35 | 1155.70 | 429.7 |
| 364.35 | 1647.70 | 654.0 |
| 364.35 | 2259.60 | 995.3 |
| 364.36 | 119.10 | 39.9 |
| 364.36 | 180.20 | 60.7 |
| 364.36 | 272.10 | 92.4 |
| 364.36 | 409.00 | 140.7 |
| 364.36 | 610.70 | 214.1 |
| 364.36 | 901.90 | 325.9 |
| 364.36 | 1309.20 | 496.0 |
| 364.36 | 1848.50 | 755.0 |
| 364.36 | 2485.70 | 1149.1 |
| 369.49 | 86.20 | 28.1 |
| 369.49 | 130.50 | 42.7 |
| 369.49 | 197.00 | 65.0 |
| 369.49 | 296.60 | 98.9 |
| 369.49 | 444.60 | 150.5 |
| 369.49 | 661.60 | 229.1 |
| 369.49 | 973.60 | 348.7 |
| 369.49 | 1407.00 | 530.7 |
| 369.49 | 1975.90 | 807.7 |
| 374.64 | 132.60 | 42.8 |
| 374.64 | 200.40 | 65.2 |
| 374.64 | 302.10 | 99.3 |
| 374.64 | 453.20 | 151.1 |
| 374.64 | 675.10 | 229.9 |
| 374.64 | 994.80 | 350.0 |
| 374.64 | 1440.50 | 532.6 |
| 374.64 | 2029.10 | 810.7 |
| 374.64 | 2729.90 | 1233.8 |
| 379.80 | 103.80 | 33.1 |
| 379.80 | 157.10 | 50.3 |
| 379.80 | 237.50 | 76.6 |
| 379.80 | 357.90 | 116.6 |
| 379.80 | 536.50 | 177.5 |
| 379.80 | 797.90 | 270.1 |
| 379.80 | 1171.80 | 411.1 |
| 379.80 | 1687.20 | 625.7 |
| 379.80 | 2352.90 | 952.3 |
| 379.80 | 3118.30 | 1449.4 |
| 384.95 | 128.90 | 40.7 |
| 384.95 | 195.10 | 62.0 |
| 384.95 | 294.60 | 94.3 |
| 384.95 | 443.10 | 143.6 |
| 384.95 | 662.20 | 218.5 |
| 384.95 | 980.30 | 332.6 |
| 384.95 | 1429.40 | 506.2 |
| 384.95 | 2045.70 | 770.4 |
| 384.95 | 2791.00 | 1172.5 |
| 384.95 | 3591.80 | 1784.6 |
| 390.14 | 197.50 | 61.7 |
| 390.14 | 298.40 | 94.0 |
| 390.14 | 448.90 | 143.0 |
| 390.14 | 671.40 | 217.7 |
| 390.14 | 995.20 | 331.4 |
| 390.14 | 1454.00 | 504.3 |
| 390.14 | 2077.00 | 767.6 |
| 390.14 | 2861.50 | 1168.2 |
| 390.14 | 3721.90 | 1778.0 |
| 390.15 | 224.40 | 69.7 |
| 390.15 | 338.00 | 106.2 |
| 390.15 | 507.00 | 161.6 |
| 390.15 | 755.40 | 245.9 |
| 390.15 | 1113.40 | 374.3 |
| 390.15 | 1614.40 | 569.6 |
| 390.15 | 2291.30 | 867.0 |
| 390.15 | 3094.90 | 1319.5 |
| 390.15 | 3936.50 | 2008.2 |
| 393.24 | 147.70 | 45.5 |
| 393.24 | 223.50 | 69.2 |
| 393.24 | 337.30 | 105.4 |
| 393.24 | 506.70 | 160.4 |
| 393.24 | 756.10 | 244.1 |
| 393.24 | 1116.90 | 371.5 |
| 393.24 | 1623.80 | 565.4 |
| 393.24 | 2302.30 | 860.5 |
| 393.24 | 3137.70 | 1309.6 |
| 393.24 | 4015.20 | 1993.2 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Thermal conductivity, W/m/K - Gas |
| 266.62 | 148.10 | 0.0135 |
| 267.77 | 148.10 | 0.0136 |
| 268.94 | 148.10 | 0.0136 |
| 276.20 | 155.80 | 0.0147 |
| 276.20 | 207.50 | 0.0147 |
| 277.09 | 207.50 | 0.0148 |
| 277.12 | 155.80 | 0.0148 |
| 278.14 | 155.80 | 0.0148 |
| 278.17 | 207.50 | 0.0149 |
| 285.91 | 253.20 | 0.0159 |
| 286.05 | 144.60 | 0.0159 |
| 286.67 | 253.20 | 0.0160 |
| 286.89 | 144.60 | 0.0160 |
| 287.68 | 253.20 | 0.0161 |
| 287.99 | 144.60 | 0.0161 |
| 295.96 | 253.20 | 0.0173 |
| 296.02 | 352.90 | 0.0173 |
| 296.03 | 154.50 | 0.0171 |
| 296.69 | 352.90 | 0.0174 |
| 296.76 | 253.20 | 0.0173 |
| 296.80 | 154.50 | 0.0173 |
| 297.39 | 352.90 | 0.0174 |
| 297.64 | 253.20 | 0.0174 |
| 297.76 | 154.50 | 0.0173 |
| 305.64 | 155.20 | 0.0183 |
| 305.64 | 502.40 | 0.0185 |
| 305.80 | 352.80 | 0.0184 |
| 306.69 | 155.20 | 0.0184 |
| 306.69 | 502.40 | 0.0186 |
| 306.80 | 352.80 | 0.0185 |
| 307.53 | 155.20 | 0.0185 |
| 307.53 | 502.40 | 0.0187 |
| 307.82 | 352.80 | 0.0186 |
| 315.68 | 496.30 | 0.0196 |
| 315.77 | 348.90 | 0.0195 |
| 316.05 | 153.90 | 0.0196 |
| 316.35 | 700.40 | 0.0201 |
| 316.55 | 496.30 | 0.0197 |
| 316.56 | 700.40 | 0.0199 |
| 316.75 | 348.90 | 0.0197 |
| 317.06 | 153.90 | 0.0196 |
| 317.20 | 700.40 | 0.0200 |
| 317.63 | 496.30 | 0.0198 |
| 317.81 | 348.90 | 0.0198 |
| 318.26 | 153.90 | 0.0197 |
| 325.16 | 1120.20 | 0.0214 |
| 325.31 | 883.70 | 0.0212 |
| 325.41 | 701.60 | 0.0210 |
| 325.53 | 500.80 | 0.0209 |
| 325.64 | 348.00 | 0.0208 |
| 325.83 | 151.50 | 0.0208 |
| 325.88 | 1120.20 | 0.0214 |
| 326.11 | 883.70 | 0.0213 |
| 326.20 | 701.60 | 0.0211 |
| 326.36 | 500.80 | 0.0210 |
| 326.53 | 348.00 | 0.0209 |
| 326.73 | 1120.20 | 0.0216 |
| 326.79 | 151.50 | 0.0209 |
| 326.99 | 883.70 | 0.0215 |
| 327.16 | 701.60 | 0.0213 |
| 327.38 | 500.80 | 0.0212 |
| 327.53 | 348.00 | 0.0210 |
| 327.88 | 151.50 | 0.0209 |
| 335.18 | 1196.90 | 0.0226 |
| 335.35 | 898.70 | 0.0224 |
| 335.43 | 705.20 | 0.0221 |
| 335.48 | 353.40 | 0.0220 |
| 335.54 | 505.20 | 0.0220 |
| 335.66 | 152.20 | 0.0220 |
| 335.88 | 1196.90 | 0.0227 |
| 336.11 | 898.70 | 0.0224 |
| 336.23 | 705.20 | 0.0223 |
| 336.32 | 353.40 | 0.0221 |
| 336.37 | 505.20 | 0.0222 |
| 336.45 | 1196.90 | 0.0228 |
| 336.55 | 152.20 | 0.0221 |
| 336.74 | 898.70 | 0.0225 |
| 336.91 | 705.20 | 0.0223 |
| 337.06 | 505.20 | 0.0223 |
| 337.25 | 353.40 | 0.0222 |
| 337.54 | 152.20 | 0.0221 |
| 345.11 | 1503.90 | 0.0242 |
| 345.23 | 1200.40 | 0.0239 |
| 345.35 | 897.30 | 0.0235 |
| 345.47 | 700.00 | 0.0234 |
| 345.57 | 502.50 | 0.0234 |
| 345.59 | 1503.90 | 0.0243 |
| 345.67 | 352.70 | 0.0234 |
| 345.74 | 1200.40 | 0.0240 |
| 345.88 | 154.30 | 0.0232 |
| 345.90 | 897.30 | 0.0236 |
| 346.03 | 700.00 | 0.0235 |
| 346.12 | 1503.90 | 0.0244 |
| 346.15 | 502.50 | 0.0235 |
| 346.26 | 352.70 | 0.0234 |
| 346.29 | 1200.40 | 0.0241 |
| 346.49 | 897.30 | 0.0237 |
| 346.52 | 154.30 | 0.0232 |
| 346.64 | 700.00 | 0.0236 |
| 346.82 | 502.50 | 0.0236 |
| 346.93 | 352.70 | 0.0235 |
| 347.27 | 154.30 | 0.0233 |
| 354.82 | 2226.00 | 0.0264 |
| 355.11 | 1777.80 | 0.0257 |
| 355.20 | 1497.30 | 0.0254 |
| 355.22 | 2226.00 | 0.0265 |
| 355.33 | 1194.90 | 0.0251 |
| 355.47 | 872.50 | 0.0248 |
| 355.55 | 701.60 | 0.0247 |
| 355.58 | 1777.80 | 0.0259 |
| 355.64 | 504.30 | 0.0247 |
| 355.66 | 2226.00 | 0.0263 |
| 355.69 | 1497.30 | 0.0255 |
| 355.74 | 356.10 | 0.0246 |
| 355.82 | 1194.90 | 0.0251 |
| 355.89 | 156.10 | 0.0244 |
| 355.97 | 872.50 | 0.0249 |
| 356.09 | 1777.80 | 0.0260 |
| 356.10 | 701.60 | 0.0249 |
| 356.20 | 504.30 | 0.0249 |
| 356.21 | 1497.30 | 0.0255 |
| 356.31 | 356.10 | 0.0248 |
| 356.38 | 1194.90 | 0.0252 |
| 356.52 | 156.10 | 0.0245 |
| 356.57 | 872.50 | 0.0250 |
| 356.72 | 701.60 | 0.0249 |
| 356.86 | 504.30 | 0.0249 |
| 356.98 | 356.10 | 0.0248 |
| 357.23 | 156.10 | 0.0246 |
| 364.94 | 2198.10 | 0.0278 |
| 365.09 | 1801.90 | 0.0269 |
| 365.20 | 1500.10 | 0.0265 |
| 365.30 | 1202.00 | 0.0262 |
| 365.42 | 906.20 | 0.0261 |
| 365.51 | 697.20 | 0.0260 |
| 365.51 | 2198.10 | 0.0279 |
| 365.59 | 481.60 | 0.0260 |
| 365.68 | 346.30 | 0.0259 |
| 365.70 | 1801.90 | 0.0271 |
| 365.81 | 1500.10 | 0.0267 |
| 365.86 | 156.40 | 0.0260 |
| 365.94 | 1202.00 | 0.0263 |
| 365.99 | 2198.10 | 0.0280 |
| 366.10 | 906.20 | 0.0261 |
| 366.20 | 697.20 | 0.0261 |
| 366.23 | 1801.90 | 0.0272 |
| 366.31 | 481.60 | 0.0260 |
| 366.35 | 1500.10 | 0.0267 |
| 366.42 | 346.30 | 0.0260 |
| 366.52 | 1202.00 | 0.0264 |
| 366.66 | 156.40 | 0.0259 |
| 366.70 | 906.20 | 0.0262 |
| 366.82 | 697.20 | 0.0261 |
| 366.96 | 481.60 | 0.0261 |
| 367.09 | 346.30 | 0.0260 |
| 367.38 | 156.40 | 0.0260 |
| 374.95 | 2704.40 | 0.0303 |
| 375.17 | 2197.80 | 0.0289 |
| 375.29 | 1766.80 | 0.0283 |
| 375.36 | 1499.60 | 0.0278 |
| 375.46 | 892.80 | 0.0273 |
| 375.49 | 1198.60 | 0.0276 |
| 375.49 | 2704.40 | 0.0304 |
| 375.54 | 707.60 | 0.0274 |
| 375.63 | 507.40 | 0.0273 |
| 375.72 | 354.00 | 0.0273 |
| 375.76 | 2197.80 | 0.0291 |
| 375.90 | 152.40 | 0.0271 |
| 375.92 | 1766.80 | 0.0283 |
| 375.95 | 2704.40 | 0.0305 |
| 375.97 | 1499.60 | 0.0279 |
| 376.14 | 892.80 | 0.0276 |
| 376.17 | 1198.60 | 0.0277 |
| 376.22 | 707.60 | 0.0275 |
| 376.28 | 2197.80 | 0.0292 |
| 376.35 | 507.40 | 0.0274 |
| 376.45 | 354.00 | 0.0274 |
| 376.46 | 1766.80 | 0.0284 |
| 376.56 | 1499.60 | 0.0279 |
| 376.68 | 152.40 | 0.0273 |
| 376.72 | 892.80 | 0.0276 |
| 376.75 | 1198.60 | 0.0277 |
| 376.81 | 707.60 | 0.0275 |
| 376.96 | 507.40 | 0.0274 |
| 377.08 | 354.00 | 0.0274 |
| 377.40 | 152.40 | 0.0273 |
| 384.94 | 3297.70 | 0.0333 |
| 385.16 | 2700.70 | 0.0312 |
| 385.35 | 2197.00 | 0.0300 |
| 385.44 | 3297.70 | 0.0335 |
| 385.48 | 1805.70 | 0.0295 |
| 385.56 | 1500.60 | 0.0292 |
| 385.66 | 1201.30 | 0.0290 |
| 385.74 | 2700.70 | 0.0313 |
| 385.77 | 899.90 | 0.0289 |
| 385.93 | 503.90 | 0.0286 |
| 385.95 | 703.00 | 0.0288 |
| 385.98 | 2197.00 | 0.0301 |
| 386.00 | 3297.70 | 0.0336 |
| 386.01 | 355.60 | 0.0286 |
| 386.13 | 1805.70 | 0.0296 |
| 386.20 | 156.60 | 0.0285 |
| 386.22 | 1500.60 | 0.0293 |
| 386.33 | 1201.30 | 0.0292 |
| 386.38 | 2700.70 | 0.0314 |
| 386.48 | 899.90 | 0.0290 |
| 386.50 | 2197.00 | 0.0302 |
| 386.60 | 703.00 | 0.0289 |
| 386.65 | 503.90 | 0.0287 |
| 386.65 | 1805.70 | 0.0296 |
| 386.74 | 1500.60 | 0.0294 |
| 386.79 | 355.60 | 0.0287 |
| 386.93 | 1201.30 | 0.0292 |
| 387.03 | 156.60 | 0.0286 |
| 387.08 | 899.90 | 0.0290 |
| 387.21 | 703.00 | 0.0290 |
| 387.32 | 503.90 | 0.0288 |
| 387.44 | 355.60 | 0.0288 |
| 387.74 | 156.60 | 0.0286 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Thermal conductivity, W/m/K - Liquid |
| 234.04 | 5100.00 | 0.1561 |
| 234.20 | 600.00 | 0.1534 |
| 234.29 | 600.00 | 0.1530 |
| 234.33 | 10000.00 | 0.1600 |
| 234.43 | 29800.00 | 0.1704 |
| 234.44 | 30000.00 | 0.1709 |
| 234.58 | 600.00 | 0.1538 |
| 234.66 | 5300.00 | 0.1568 |
| 234.70 | 20200.00 | 0.1655 |
| 234.71 | 10400.00 | 0.1605 |
| 234.72 | 5300.00 | 0.1562 |
| 234.79 | 30100.00 | 0.1703 |
| 235.00 | 20100.00 | 0.1654 |
| 235.27 | 20200.00 | 0.1655 |
| 235.32 | 10700.00 | 0.1598 |
| 253.99 | 10200.00 | 0.1528 |
| 254.02 | 600.00 | 0.1422 |
| 254.11 | 20400.00 | 0.1582 |
| 254.12 | 30200.00 | 0.1633 |
| 254.16 | 600.00 | 0.1427 |
| 254.20 | 20100.00 | 0.1579 |
| 254.22 | 10400.00 | 0.1529 |
| 254.34 | 30300.00 | 0.1643 |
| 254.37 | 20100.00 | 0.1583 |
| 254.42 | 600.00 | 0.1427 |
| 254.42 | 5100.00 | 0.1467 |
| 254.81 | 10100.00 | 0.1522 |
| 254.88 | 5100.00 | 0.1466 |
| 255.08 | 5000.00 | 0.1471 |
| 257.35 | 29900.00 | 0.1640 |
| 273.93 | 5000.00 | 0.1396 |
| 274.08 | 5100.00 | 0.1396 |
| 274.48 | 5000.00 | 0.1404 |
| 274.56 | 29800.00 | 0.1585 |
| 274.57 | 30400.00 | 0.1579 |
| 274.60 | 20000.00 | 0.1523 |
| 274.90 | 10500.00 | 0.1456 |
| 274.90 | 20300.00 | 0.1522 |
| 275.12 | 20300.00 | 0.1523 |
| 275.22 | 10200.00 | 0.1452 |
| 275.30 | 30600.00 | 0.1582 |
| 275.31 | 700.00 | 0.1342 |
| 275.74 | 700.00 | 0.1343 |
| 276.02 | 10500.00 | 0.1459 |
| 276.44 | 700.00 | 0.1347 |
| 293.79 | 5100.00 | 0.1305 |
| 293.80 | 800.00 | 0.1249 |
| 294.15 | 800.00 | 0.1252 |
| 294.16 | 10000.00 | 0.1362 |
| 294.22 | 10200.00 | 0.1364 |
| 294.30 | 29800.00 | 0.1495 |
| 294.45 | 800.00 | 0.1248 |
| 294.45 | 4900.00 | 0.1305 |
| 294.59 | 29900.00 | 0.1486 |
| 294.68 | 20600.00 | 0.1417 |
| 294.84 | 5200.00 | 0.1307 |
| 295.13 | 20300.00 | 0.1417 |
| 295.22 | 10000.00 | 0.1356 |
| 296.32 | 20200.00 | 0.1415 |
| 314.01 | 5100.00 | 0.1191 |
| 314.06 | 1000.00 | 0.1143 |
| 314.11 | 5200.00 | 0.1189 |
| 314.39 | 1000.00 | 0.1145 |
| 314.39 | 5100.00 | 0.1195 |
| 314.43 | 10200.00 | 0.1242 |
| 314.60 | 30100.00 | 0.1385 |
| 314.66 | 1000.00 | 0.1137 |
| 314.81 | 10200.00 | 0.1241 |
| 314.88 | 30000.00 | 0.1382 |
| 315.01 | 20400.00 | 0.1313 |
| 315.06 | 10100.00 | 0.1242 |
| 315.07 | 20100.00 | 0.1318 |
| 315.37 | 30400.00 | 0.1384 |
| 315.55 | 20000.00 | 0.1318 |
| 333.73 | 1500.00 | 0.1079 |
| 333.92 | 5200.00 | 0.1113 |
| 334.03 | 1500.00 | 0.1075 |
| 334.09 | 30000.00 | 0.1283 |
| 334.31 | 20200.00 | 0.1229 |
| 334.38 | 30100.00 | 0.1287 |
| 334.47 | 1500.00 | 0.1078 |
| 334.55 | 5100.00 | 0.1108 |
| 334.70 | 10200.00 | 0.1156 |
| 334.79 | 20200.00 | 0.1224 |
| 334.85 | 5200.00 | 0.1116 |
| 334.90 | 30200.00 | 0.1288 |
| 334.91 | 10200.00 | 0.1154 |
| 335.09 | 30400.00 | 0.1294 |
| 335.29 | 20100.00 | 0.1228 |
| 335.37 | 10100.00 | 0.1151 |
| 335.72 | 20000.00 | 0.1223 |
| 335.76 | 10300.00 | 0.1146 |
| 353.73 | 10300.00 | 0.1059 |
| 353.93 | 30500.00 | 0.1206 |
| 353.97 | 30100.00 | 0.1208 |
| 354.06 | 10200.00 | 0.1053 |
| 354.10 | 20400.00 | 0.1145 |
| 354.15 | 5800.00 | 0.0998 |
| 354.21 | 2300.00 | 0.0973 |
| 354.29 | 5300.00 | 0.1005 |
| 354.45 | 2300.00 | 0.0970 |
| 354.59 | 30100.00 | 0.1208 |
| 354.86 | 2300.00 | 0.0971 |
| 354.97 | 5200.00 | 0.1000 |
| 355.08 | 20000.00 | 0.1141 |
| 355.18 | 2300.00 | 0.0971 |
| 355.36 | 20100.00 | 0.1142 |
| 355.46 | 5200.00 | 0.1012 |
| 374.25 | 10700.00 | 0.0988 |
| 374.25 | 20500.00 | 0.1071 |
| 374.30 | 30400.00 | 0.1129 |
| 374.62 | 30300.00 | 0.1133 |
| 374.81 | 29900.00 | 0.1135 |
| 374.85 | 3300.00 | 0.0871 |
| 374.85 | 5100.00 | 0.0908 |
| 374.91 | 5000.00 | 0.0908 |
| 375.13 | 3300.00 | 0.0869 |
| 375.27 | 5000.00 | 0.0911 |
| 375.38 | 3300.00 | 0.0867 |
| 375.68 | 20200.00 | 0.1065 |
| 376.02 | 20000.00 | 0.1065 |
| 376.38 | 10600.00 | 0.0976 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 5094.52] | kPa | [179.07; 400.38] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44577e+01 | |||
| Coefficient B | -2.25150e+03 | |||
| Coefficient C | -2.01740e+01 | |||
| Temperature range, min. | 179.07 | |||
| Temperature range, max. | 400.38 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 | ||||
| Pvap | 1.33 | kPa | 179.07 | Calculated Property |
| Pvap | 8.91 | kPa | 203.66 | Calculated Property |
| Pvap | 37.98 | kPa | 228.25 | Calculated Property |
| Pvap | 119.19 | kPa | 252.84 | Calculated Property |
| Pvap | 300.58 | kPa | 277.43 | Calculated Property |
| Pvap | 645.04 | kPa | 302.02 | Calculated Property |
| Pvap | 1224.56 | kPa | 326.61 | Calculated Property |
| Pvap | 2113.56 | kPa | 351.20 | Calculated Property |
| Pvap | 3382.75 | kPa | 375.79 | Calculated Property |
| Pvap | 5094.52 | kPa | 400.38 | Calculated Property |
| Pvap | [3.05e-03; 5229.57] | kPa | [131.65; 400.10] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.55657e+01 | |||
| Coefficient B | -3.69518e+03 | |||
| Coefficient C | -4.79328e+00 | |||
| Coefficient D | 5.94662e-06 | |||
| Temperature range, min. | 131.65 | |||
| Temperature range, max. | 400.10 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 | ||||
| Pvap | 3.05e-03 | kPa | 131.65 | Calculated Property |
| Pvap | 0.22 | kPa | 161.48 | Calculated Property |
| Pvap | 3.61 | kPa | 191.31 | Calculated Property |
| Pvap | 26.27 | kPa | 221.13 | Calculated Property |
| Pvap | 113.51 | kPa | 250.96 | Calculated Property |
| Pvap | 347.93 | kPa | 280.79 | Calculated Property |
| Pvap | 842.78 | kPa | 310.62 | Calculated Property |
| Pvap | 1728.42 | kPa | 340.44 | Calculated Property |
| Pvap | 3142.63 | kPa | 370.27 | Calculated Property |
| Pvap | 5229.57 | kPa | 400.10 | Calculated Property |
Similar Compounds
Find more compounds similar to Dimethyl ether.
Mixtures
- Norflurane + Dimethyl ether
- Ethane, 1,1,1-trifluoro- + Dimethyl ether
- Carbon dioxide + Dimethyl ether
- Dimethyl ether + Water
- Carbon dioxide + Dimethyl ether + Water
- Propane + Dimethyl ether
- Butane, decafluoro- + Dimethyl ether
- Dimethyl sulfide + Dimethyl ether
- Dimethyl ether + Methane, iodo-
- Ethane, pentafluoro- + Dimethyl ether
- Butane + Dimethyl ether
- Dimethyl ether + Isobutane
- Difluoromethane + Dimethyl ether
- Propene + Dimethyl ether
- Dimethyl ether + Methyl Alcohol
- Ethanol + Dimethyl ether
- 1-Propanol + Dimethyl ether
- 1-Butanol + Dimethyl ether
- Dimethyl ether + Methyl Alcohol + Water
- Methyl formate + Dimethyl ether
Find more mixtures with Dimethyl ether.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Measurement of Vapor Liquid Equilibrium for the DME + Diisopropyl Ether Binary System and Correlation for the DME + CO2 + Diisopropyl Ether Ternary System
- Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
- Vapor liquid equilibrium data for the difluoromethane (R32) dimethyl ether (RE170) system at temperatures from 283.03 to 363.21K and pressures up to 5.5MPa
- Experimental densities, vapor pressures, and critical point, and a fundamental equation of state for dimethyl ether
- Vapor liquid equilibria of the 1,1,1-trifluoroethane (HFC-143a) + dimethyl ether (DME) system
- The solubility of water in mixtures of dimethyl ether and carbon dioxide
- Surface tension of dimethyl ether + propane from 243 to 333 K
- Gas phase PVT properties and second virial coefficients of dimethyl ether
- Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
- Vapor-liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method
- Isothermal vapor-liquid equilibria for the binary system of dimethylether (DME) + methyl iodide (CH3I)
- Measurement and correlation of solid-liquid equilibria for three binaries, ethanol-antipyrine, chloroform-antipyrine, and dimethyl ether-antipyrine
- Capillary constant and surface tension of dimethyl ether and n-butane at temperatures from 214 K to those close to the critical point
- Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
- (Vapour + liquid) equilibria of the {pentafluoroethane (HFC-125) + dimethyl ether (DME)} system
- Compressed liquid density measurements of dimethyl ether with a vibrating tube densimeter
- Solubility of dimethyl ether in pentaerythritol tetrabutyrate and in pentaerythritol tetrapentanoate. Comparison with other pentaerythritol tetraalkyl esters
- Experimental Study of PVTx Properties in the Gas Phase for Binary Mixtures of DME and HFC-134a
- Phase Equilibrium Behavior for Methoxymethane + Pentaerythritol Tetraheptanoate and Methoxymethane + Pentaerythritol Tetranonanoate Systems
- Heat Capacity of Saturated and Compressed Liquid Dimethyl Ether at Temperatures from (132 to 345) K and at Pressures to 35 MPa
- Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
- VLE and VLLE Measurements of Dimethyl Ether Containing Systems. 2
- Viscosity of saturated liquid dimethyl ether from ( 227 to 343 ) K
- Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Propane + Dimethyl Ether and Propene + Dimethyl Ether at Temperatures from (298 to 323) K
- Vapor Pressure Measurements of Dimethyl Ether from (233 to 399) K
- Surface Tension of Dimethyl Ether from (213 to 368) K
- Measurement of the Critical Parameters and the Saturation Densities of Dimethyl Ether
- Critical Properties of Three Dimethyl Ether Binary Systems: Dimethyl Ether (RE-170) + Propane (HC-290), Butane (HC-600), and 2-Methyl Propane (HC-600A)
- Isothermal VLE Measurements for Difluoromethane + Dimethylether and an Evaluation of Hydrogen Bonding
- Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
- Compressed Liquid Densities and Saturated Liquid Densities of Dimethyl Ether (RE170)
- Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Propen-1-ol
- Thermal Conductivity of Gaseous Dimethyl Ether from (263 to 383) K
- Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
- Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methyl-3-buten-2-ol and 3-Methyl-3-buten-1-ol
- Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
- Saturated Pressure Measurements of Dimethyl Ether at Temperatures from (219 to 361) K
- Vapor-Liquid Equilibria and HE for Binary Systems of Dimethyl Ether (DME) with C1-C4 Alkan-1-ols at 323.15 K and Liquid-Liquid Equilibria for Ternary System of DME + Methanol + Water at 313.15 K
- Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
- Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
- Vapor-Liquid Equilibrium for Methoxymethane + Methyl Formate, Methoxymethane + Hexane, and Methyl Formate + Methanol
- Experimental Measurement and Modeling of the Viscosity of Dimethyl Ether
- Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol
- Bubble-Point Measurements of Eight Binary Mixtures for Organic Rankine Cycle Applications
- Isobaric Heat Capacity Measurements for Dimethyl Ether and 1,1-Difluoroethane in the Liquid Phase at Temperatures from 305 K to 365 K and Pressures up to 5 MPa
- Solubility of Dimethyl Ether in Pentaerythritol Tetrahexanoate (PEC6) and in Pentaerythritol Tetraoctanoate (PEC8) Between (283.15 and 353.15) K
- Isothermal Vapor-liquid Equilibrium of the ternary mixture of 1,1,1,2-tetrafluoroethane + 2,3,3,3-tetrafluoroprop-1- ene + dimethylether at temperatures from 253.15 to 323.15 K
- Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
- Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
- Phase Equilibrium of Biodiesel Compounds for the Triolein + Palmitic Acid + Methanol System with Dimethyl Ether as Cosolvent
- Vapor-Liquid Equilibrium Data of the Binary Systems in Oxidative Carbonylation of Dimethyl Ether Synthesizing Dimethyl Carbonate
- Vapor Pressure Measurements of Dimethyl Ether from (213 to 393) K
- Second Virial Coefficients for Dimethyl Ether
- Viscosity of Gaseous Mixtures of Methoxymethane + Nitrogen
- Thermal Conductivity of Liquid Dimethyl Ether from (233 to 373) K at Pressures up to 30 MPa
- Measurements of the Isobaric Specific Heat Capacity and Density for Dimethyl Ether in the Liquid State
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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