- InChI
- InChI=1S/C4H10/c1-3-4-2/h3-4H2,1-2H3
- InChI Key
- IJDNQMDRQITEOD-UHFFFAOYSA-N
- Formula
- C4H10
- SMILES
- CCCC
- Molecular Weight1
- 58.12
- CAS
- 106-97-8
- Other Names
-
- A 21
- Butanen
- Butani
- DIETHYL
- Freon 600
- HC 600
- HC 600 (hydrocarbon)
- LPG
- Liquefied petroleum gas
- Methylethylmethane
- R 600
- R 600 (alkane)
- UN 1011
- n-Butane
- n-C4H10
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- AP : Aniline Point (K).
- 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).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (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).
- ΔsubH : Enthalpy of sublimation 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- 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).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 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 | 0.1990 | KDB | |
| Tig | 703.71 | K | KDB |
| AP | 356.250 | K | KDB |
| ΔcH°gas | [-2878.30; -2876.20] | kJ/mol |
|
| ΔcH°gas | -2877.50 ± 0.63 | kJ/mol | NIST |
| ΔcH°gas | -2876.20 ± 0.63 | kJ/mol | NIST |
| ΔcH°gas | -2878.30 ± 0.63 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| LFL | 1.80 | % in Air | KDB |
| UFL | 8.40 | % in Air | KDB |
| Tflash,oc | 199.82 | K | KDB |
| ΔfG° | -16.10 | kJ/mol | KDB |
| Rg | 2.8890 | KDB | |
| Δc,grossH | 2855.37 | kJ/mol | KDB |
| Δc,netH | 2635.334 | kJ/mol | KDB |
| ΔfH°gas | [-127.10; -125.60] | kJ/mol |
|
| ΔfH°gas | -126.20 | kJ/mol | KDB |
| ΔfH°gas | -125.60 ± 0.67 | kJ/mol | NIST |
| ΔfH°gas | -127.10 ± 0.67 | kJ/mol | NIST |
| ΔfusH° | 6.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 22.40 | kJ/mol | NIST |
| IE | [10.35; 11.20] | eV |
|
| IE | 10.53 ± 0.02 | eV | NIST |
| IE | 10.57 | eV | NIST |
| IE | 10.53 ± 0.10 | eV | NIST |
| IE | 10.35 ± 0.15 | eV | NIST |
| IE | 10.60 ± 0.10 | eV | NIST |
| IE | 10.61 | eV | NIST |
| IE | 10.87 ± 0.05 | eV | NIST |
| IE | 10.89 | eV | NIST |
| IE | 10.67 | eV | NIST |
| IE | 10.55 ± 0.05 | eV | NIST |
| IE | 10.50 | eV | NIST |
| IE | 10.55 ± 0.05 | eV | NIST |
| IE | 10.63 ± 0.03 | eV | NIST |
| IE | 11.09 | eV | NIST |
| IE | 11.20 | eV | NIST |
| IE | 11.20 ± 0.10 | eV | NIST |
| log10WS | [-2.72; -2.57] |
|
|
| log10WS | -2.72 | Aq. Sol... | |
| log10WS | -2.57 | Estimat... | |
| logPoct/wat | 1.806 | Crippen Calculated Property | |
| McVol | 67.220 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 4 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3787.00; 3796.00] | kPa |
|
| Pc | 3796.00 | kPa | KDB |
| Pc | 3787.00 | kPa | Critica... |
| Ptriple | [7.00e-04; 7.00e-04] | kPa |
|
| Ptriple | 7.00e-04 ± 8.00e-07 | kPa | NIST |
| Ptriple | 7.00e-04 | kPa | NIST |
| S°liquid | [226.80; 231.00] | J/mol×K |
|
| S°liquid | 231.00 | J/mol×K | NIST |
| S°liquid | 226.80 | J/mol×K | NIST |
| S°liquid | 229.70 | J/mol×K | NIST |
| Tboil | 272.60 | K | KDB |
| Tc | [423.90; 426.35] | K |
|
| Tc | 425.12 | K | KDB |
| Tc | 424.82 | K | Validat... |
| Tc | 425.10 ± 0.10 | K | NIST |
| Tc | 425.12 ± 0.20 | K | NIST |
| Tc | 425.18 | K | NIST |
| Tc | 425.16 ± 0.10 | K | NIST |
| Tc | 425.10 ± 0.10 | K | NIST |
| Tc | 424.65 ± 0.50 | K | NIST |
| Tc | 425.16 ± 0.07 | K | NIST |
| Tc | 425.16 | K | NIST |
| Tc | 425.12 ± 0.10 | K | NIST |
| Tc | 425.35 ± 0.20 | K | NIST |
| Tc | 425.40 ± 0.40 | K | NIST |
| Tc | 425.12 ± 0.20 | K | NIST |
| Tc | 425.37 ± 0.55 | K | NIST |
| Tc | 425.40 ± 1.11 | K | NIST |
| Tc | 425.16 ± 0.03 | K | NIST |
| Tc | Outlier 423.90 ± 2.00 | K | NIST |
| Tc | Outlier 426.35 ± 0.50 | K | NIST |
| Tc | Outlier 424.00 ± 1.00 | K | NIST |
| Tfus | [134.86; 135.23] | K |
|
| Tfus | 134.86 | K | KDB |
| Tfus | 135.23 | K | Aq. Sol... |
| Ttriple | 134.86 | K | KDB |
| Vc | [0.255; 0.263] | m3/kmol |
|
| Vc | 0.255 | m3/kmol | KDB |
| Vc | 0.255 | m3/kmol | NIST |
| Vc | 0.263 ± 0.010 | m3/kmol | NIST |
| Vc | 0.255 ± 0.001 | m3/kmol | NIST |
| Vc | 0.258 ± 0.003 | m3/kmol | NIST |
| Zc | 0.2738530 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [110.58; 185.85] | J/mol×K | [344.90; 692.60] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 120 140 160 180 400 500 600 700 | ||||
| Cp,gas | 110.58 | J/mol×K | 344.90 | NIST |
| Cp,gas | 114.93 | J/mol×K | 359.60 | NIST |
| Cp,gas | 121.75 | J/mol×K | 387.50 | NIST |
| Cp,gas | 137.99 | J/mol×K | 451.60 | NIST |
| Cp,gas | 154.01 | J/mol×K | 521.00 | NIST |
| Cp,gas | 162.26 | J/mol×K | 561.30 | NIST |
| Cp,gas | 170.33 | J/mol×K | 600.80 | NIST |
| Cp,gas | 185.85 | J/mol×K | 692.60 | NIST |
| Cp,liquid | [129.70; 132.42] | J/mol×K | [261.80; 270.00] |
|
| Cp,liquid | 129.70 | J/mol×K | 261.80 | NIST |
| Cp,liquid | 132.42 | J/mol×K | 270.00 | NIST |
| η | [0.0001816; 0.0027951] | Pa×s | [134.84; 290.92] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 150 200 250 | ||||
| η | 0.0027951 | Pa×s | 134.84 | Joback Calculated Property |
| η | 0.0012261 | Pa×s | 160.85 | Joback Calculated Property |
| η | 0.0006765 | Pa×s | 186.87 | Joback Calculated Property |
| η | 0.0004317 | Pa×s | 212.88 | Joback Calculated Property |
| η | 0.0003037 | Pa×s | 238.89 | Joback Calculated Property |
| η | 0.0002290 | Pa×s | 264.91 | Joback Calculated Property |
| η | 0.0001816 | Pa×s | 290.92 | Joback Calculated Property |
| ΔfusH | [2.07; 4.66] | kJ/mol | [107.60; 134.90] |
|
| ΔfusH | 2.07 | kJ/mol | 107.60 | NIST |
| ΔfusH | 4.66 | kJ/mol | 134.90 | NIST |
| ΔfusH | 4.66 | kJ/mol | 134.90 | NIST |
| ΔsubH | 35.90 | kJ/mol | 107.00 | NIST |
| ΔvapH | [21.00; 27.00] | kJ/mol | [174.00; 400.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 21 22 23 24 25 26 27 200 300 400 | ||||
| ΔvapH | 27.00 | kJ/mol | 174.00 | NIST |
| ΔvapH | 23.90 | kJ/mol | 234.00 | NIST |
| ΔvapH | 23.10 | kJ/mol | 242.50 | NIST |
| ΔvapH | 23.40 | kJ/mol | 243.50 | NIST |
| ΔvapH | 22.39 | kJ/mol | 272.05 | NIST |
| ΔvapH | 21.00 ± 0.08 | kJ/mol | 272.66 | NIST |
| ΔvapH | 22.44 | kJ/mol | 272.70 | NIST |
| ΔvapH | 22.39 | kJ/mol | 273.00 | KDB |
| ΔvapH | 23.20 | kJ/mol | 297.00 | NIST |
| ΔvapH | 22.90 | kJ/mol | 307.50 | NIST |
| ΔvapH | 22.60 | kJ/mol | 349.50 | NIST |
| ΔvapH | 22.80 | kJ/mol | 400.00 | NIST |
| Pvap | [1.30e-03; 3716.90] | kPa | [135.00; 424.00] |
|
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 | ||||
| Pvap | 1.30e-03 | kPa | 135.00 | Measure... |
| Pvap | 2.10e-03 | kPa | 140.00 | Measure... |
| Pvap | 9.30e-03 | kPa | 150.00 | Measure... |
| Pvap | 0.04 | kPa | 160.00 | Measure... |
| Pvap | 0.12 | kPa | 170.00 | Measure... |
| Pvap | 0.34 | kPa | 180.00 | Measure... |
| Pvap | 0.42 | kPa | 182.33 | Vapour ... |
| Pvap | 0.85 | kPa | 190.00 | Measure... |
| Pvap | 1.94 | kPa | 200.00 | Measure... |
| Pvap | 4.04 | kPa | 210.00 | Measure... |
| Pvap | 7.80 | kPa | 220.00 | Measure... |
| Pvap | 14.11 | kPa | 230.00 | Measure... |
| Pvap | 24.09 | kPa | 240.00 | Measure... |
| Pvap | 26.20 | kPa | 240.00 | Liquid-... |
| Pvap | 23.90 | kPa | 240.00 | Liquid-... |
| Pvap | 29.10 | kPa | 243.03 | Phase E... |
| Pvap | 39.16 | kPa | 250.00 | Measure... |
| Pvap | 59.90 | kPa | 260.00 | Liquid-... |
| Pvap | 60.99 | kPa | 260.00 | Measure... |
| Pvap | 69.60 | kPa | 263.15 | Vapor-L... |
| Pvap | 91.50 | kPa | 270.00 | Measure... |
| Pvap | 104.00 | kPa | 273.15 | Vapor l... |
| Pvap | 103.40 | kPa | 273.15 | Vapor-L... |
| Pvap | 104.00 | kPa | 273.15 | Vapor-L... |
| Pvap | 104.00 | kPa | 273.15 | Vapor-L... |
| Pvap | 103.00 | kPa | 273.15 | Vapor-L... |
| Pvap | 104.00 | kPa | 273.27 | Isother... |
| Pvap | 110.67 | kPa | 275.00 | Measure... |
| Pvap | 125.10 | kPa | 278.15 | Vapor-L... |
| Pvap | 131.50 | kPa | 280.00 | Liquid-... |
| Pvap | 133.00 | kPa | 280.00 | Measure... |
| Pvap | 149.00 | kPa | 283.15 | Vapor-L... |
| Pvap | 150.00 | kPa | 283.15 | Vapor l... |
| Pvap | 148.10 | kPa | 283.15 | Vapor-L... |
| Pvap | 150.00 | kPa | 283.15 | Vapor-L... |
| Pvap | 150.00 | kPa | 283.15 | Vapor-L... |
| Pvap | 148.00 | kPa | 283.15 | (Vapour... |
| Pvap | 149.00 | kPa | 283.15 | Vapor-L... |
| Pvap | 158.31 | kPa | 285.00 | Measure... |
| Pvap | 177.00 | kPa | 288.25 | Isother... |
| Pvap | 187.37 | kPa | 290.00 | Measure... |
| Pvap | 208.00 | kPa | 293.15 | (Vapour... |
| Pvap | 208.00 | kPa | 293.15 | Vapor l... |
| Pvap | 209.40 | kPa | 293.15 | Vapor-L... |
| Pvap | 208.00 | kPa | 293.15 | Vapor-L... |
| Pvap | 208.30 | kPa | 293.15 | Vapor-L... |
| Pvap | 208.00 | kPa | 293.15 | Vapor-L... |
| Pvap | 208.00 | kPa | 293.15 | Vapor-L... |
| Pvap | 207.20 | kPa | 293.15 | Vapor-L... |
| Pvap | 210.80 | kPa | 293.38 | Phase E... |
| Pvap | 215.00 | kPa | 294.23 | Isother... |
| Pvap | 231.00 | kPa | 296.23 | Isother... |
| Pvap | 257.50 | kPa | 300.00 | Measure... |
| Pvap | 256.40 | kPa | 300.00 | Liquid-... |
| Pvap | 257.62 | kPa | 300.00 | Measure... |
| Pvap | 280.00 | kPa | 302.92 | Phase e... |
| Pvap | 283.40 | kPa | 303.15 | Vapor-L... |
| Pvap | 283.70 | kPa | 303.15 | Isother... |
| Pvap | 284.00 | kPa | 303.15 | Vapor-L... |
| Pvap | 284.00 | kPa | 303.15 | Vapor-L... |
| Pvap | 284.00 | kPa | 303.15 | Vapor l... |
| Pvap | 284.00 | kPa | 303.15 | Vapor-L... |
| Pvap | 284.00 | kPa | 303.15 | Vapor-L... |
| Pvap | 282.00 | kPa | 303.15 | (Vapour... |
| Pvap | 324.00 | kPa | 307.93 | Phase e... |
| Pvap | 328.80 | kPa | 308.15 | Vapor-L... |
| Pvap | 332.00 | kPa | 308.21 | Isother... |
| Pvap | 346.30 | kPa | 310.00 | Measure... |
| Pvap | 377.00 | kPa | 312.87 | Phase e... |
| Pvap | 378.00 | kPa | 313.15 | (Vapour... |
| Pvap | 377.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 378.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 377.00 | kPa | 313.15 | (Vapour... |
| Pvap | 378.10 | kPa | 313.15 | Vapor-L... |
| Pvap | 378.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 378.60 | kPa | 313.15 | Vapor-L... |
| Pvap | 378.00 | kPa | 313.15 | Vapor l... |
| Pvap | 378.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 378.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 379.00 | kPa | 313.20 | High pr... |
| Pvap | 425.70 | kPa | 317.47 | Isother... |
| Pvap | 426.80 | kPa | 317.60 | Vapour ... |
| Pvap | 432.00 | kPa | 317.88 | Phase e... |
| Pvap | 436.20 | kPa | 318.35 | Vapor-L... |
| Pvap | 437.50 | kPa | 318.35 | Vapor-L... |
| Pvap | 436.55 | kPa | 318.40 | Vapour ... |
| Pvap | 454.80 | kPa | 320.00 | Liquid-... |
| Pvap | 456.24 | kPa | 320.00 | Measure... |
| Pvap | 456.20 | kPa | 320.00 | Measure... |
| Pvap | 479.50 | kPa | 322.01 | Phase e... |
| Pvap | 491.00 | kPa | 322.86 | Phase e... |
| Pvap | 495.00 | kPa | 323.12 | Vapor L... |
| Pvap | 495.30 | kPa | 323.13 | Vapor L... |
| Pvap | 494.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 495.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 494.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 496.50 | kPa | 323.15 | Vapor-L... |
| Pvap | 495.60 | kPa | 323.15 | Vapor L... |
| Pvap | 495.00 | kPa | 323.15 | Vapor l... |
| Pvap | 495.70 | kPa | 323.15 | Vapor L... |
| Pvap | 496.20 | kPa | 323.15 | Isother... |
| Pvap | 493.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 496.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 493.10 | kPa | 323.15 | Vapor-L... |
| Pvap | 495.00 | kPa | 323.15 | (Vapour... |
| Pvap | 498.00 | kPa | 323.19 | Isother... |
| Pvap | 561.00 | kPa | 327.88 | Phase e... |
| Pvap | 590.40 | kPa | 330.00 | Measure... |
| Pvap | 592.44 | kPa | 330.16 | Vapor-L... |
| Pvap | 632.00 | kPa | 332.83 | Phase e... |
| Pvap | 638.00 | kPa | 333.15 | Vapor-L... |
| Pvap | 638.00 | kPa | 333.15 | (Vapour... |
| Pvap | 639.00 | kPa | 333.15 | Vapor-L... |
| Pvap | 645.00 | kPa | 333.20 | High pr... |
| Pvap | 679.30 | kPa | 335.60 | Vapor-L... |
| Pvap | 677.90 | kPa | 335.60 | Vapor-L... |
| Pvap | 714.00 | kPa | 337.82 | Phase e... |
| Pvap | 752.00 | kPa | 340.00 | Measure... |
| Pvap | 751.90 | kPa | 340.00 | Measure... |
| Pvap | 750.50 | kPa | 340.00 | Liquid-... |
| Pvap | 751.00 | kPa | 340.00 | Liquid-... |
| Pvap | 804.00 | kPa | 342.82 | Phase e... |
| Pvap | 809.80 | kPa | 343.15 | Isother... |
| Pvap | 810.00 | kPa | 343.15 | Vapor-L... |
| Pvap | 810.00 | kPa | 343.15 | (Vapour... |
| Pvap | 881.70 | kPa | 346.97 | Vapor-L... |
| Pvap | 897.00 | kPa | 347.81 | Phase e... |
| Pvap | 951.70 | kPa | 350.36 | Vapor-L... |
| Pvap | 1012.00 | kPa | 353.15 | Vapor-L... |
| Pvap | 1039.00 | kPa | 353.15 | In Situ... |
| Pvap | 1012.00 | kPa | 353.15 | (Vapour... |
| Pvap | 1013.00 | kPa | 353.20 | High pr... |
| Pvap | 1170.20 | kPa | 360.00 | Measure... |
| Pvap | 1168.50 | kPa | 360.00 | Liquid-... |
| Pvap | 1168.10 | kPa | 360.00 | Liquid-... |
| Pvap | 1249.80 | kPa | 363.15 | Isother... |
| Pvap | 1249.00 | kPa | 363.15 | (Vapour... |
| Pvap | 1250.00 | kPa | 363.15 | Vapor-L... |
| Pvap | 1284.50 | kPa | 364.51 | Vapor L... |
| Pvap | 1434.90 | kPa | 370.00 | Measure... |
| Pvap | 1526.80 | kPa | 373.15 | Isother... |
| Pvap | 1586.00 | kPa | 373.15 | In Situ... |
| Pvap | 1525.00 | kPa | 373.20 | High pr... |
| Pvap | 1739.90 | kPa | 380.00 | Measure... |
| Pvap | 1737.40 | kPa | 380.00 | Liquid-... |
| Pvap | 1740.40 | kPa | 380.00 | Measure... |
| Pvap | 2092.10 | kPa | 390.00 | Measure... |
| Pvap | 2265.00 | kPa | 393.15 | In Situ... |
| Pvap | 2494.60 | kPa | 400.00 | Measure... |
| Pvap | 2495.20 | kPa | 400.00 | Measure... |
| Pvap | 2660.00 | kPa | 403.20 | High pr... |
| Pvap | 2955.00 | kPa | 410.00 | Measure... |
| Pvap | 3156.00 | kPa | 413.15 | In Situ... |
| Pvap | 3482.50 | kPa | 420.00 | Measure... |
| Pvap | 3597.50 | kPa | 422.00 | Measure... |
| Pvap | 3716.90 | kPa | 424.00 | Measure... |
| n0 | 1.32920 | 298.15 | KDB | |
| ρl | 579.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | [19.06; 34.56] | J/mol×K | [107.60; 134.90] |
|
| ΔfusS | 19.06 | J/mol×K | 107.60 | NIST |
| ΔfusS | 34.56 | J/mol×K | 134.90 | NIST |
| γ | [3.60e-05; 0.01] | N/m | [278.15; 423.04] |
|
|
T(K) Surface Tension (N/m) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 0.01 0.02 300 350 400 | ||||
| γ | 0.01 | N/m | 278.15 | Capilla... |
| γ | 0.01 | N/m | 283.15 | Capilla... |
| γ | 0.01 | N/m | 288.15 | Capilla... |
| γ | 0.01 | N/m | 293.15 | Capilla... |
| γ | 0.01 | N/m | 293.20 | KDB |
| γ | 0.01 | N/m | 298.15 | Capilla... |
| γ | 0.01 | N/m | 303.15 | Capilla... |
| γ | 0.01 | N/m | 308.15 | Capilla... |
| γ | 0.01 | N/m | 313.15 | Capilla... |
| γ | 0.01 | N/m | 318.15 | Capilla... |
| γ | 0.01 | N/m | 323.15 | Capilla... |
| γ | 0.01 | N/m | 328.15 | Capilla... |
| γ | 0.01 | N/m | 333.15 | Capilla... |
| γ | 0.01 | N/m | 338.15 | Capilla... |
| γ | 0.01 | N/m | 343.15 | Capilla... |
| γ | 0.01 | N/m | 348.15 | Capilla... |
| γ | 0.01 | N/m | 353.15 | Capilla... |
| γ | 0.01 | N/m | 358.15 | Capilla... |
| γ | 0.00 | N/m | 363.15 | Capilla... |
| γ | 0.00 | N/m | 368.15 | Capilla... |
| γ | 0.00 | N/m | 373.15 | Capilla... |
| γ | 0.00 | N/m | 378.15 | Capilla... |
| γ | 0.00 | N/m | 383.15 | Capilla... |
| γ | 0.00 | N/m | 388.15 | Capilla... |
| γ | 0.00 | N/m | 393.15 | Capilla... |
| γ | 0.00 | N/m | 398.15 | Capilla... |
| γ | 0.00 | N/m | 403.15 | Capilla... |
| γ | 9.23e-04 | N/m | 408.15 | Capilla... |
| γ | 5.83e-04 | N/m | 413.15 | Capilla... |
| γ | 3.41e-04 | N/m | 417.15 | Capilla... |
| γ | 1.86e-04 | N/m | 419.75 | Capilla... |
| γ | 1.57e-04 | N/m | 420.35 | Capilla... |
| γ | 1.29e-04 | N/m | 420.85 | Capilla... |
| γ | 1.18e-04 | N/m | 421.08 | Capilla... |
| γ | 1.00e-04 | N/m | 421.48 | Capilla... |
| γ | 8.10e-05 | N/m | 421.88 | Capilla... |
| γ | 6.40e-05 | N/m | 422.28 | Capilla... |
| γ | 5.10e-05 | N/m | 422.63 | Capilla... |
| γ | 3.60e-05 | N/m | 423.04 | Capilla... |
| ΔvapS | 82.30 | J/mol×K | 272.05 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 273.15 | 100.00 | 0.0002 |
| 273.15 | 10000.00 | 0.0002 |
| 273.15 | 20000.00 | 0.0002 |
| 273.15 | 30000.00 | 0.0003 |
| 293.15 | 200.00 | 0.0002 |
| 293.15 | 10000.00 | 0.0002 |
| 293.15 | 20000.00 | 0.0002 |
| 293.15 | 30000.00 | 0.0002 |
| 313.15 | 400.00 | 0.0001 |
| 313.15 | 10000.00 | 0.0002 |
| 313.15 | 20000.00 | 0.0002 |
| 313.15 | 30000.00 | 0.0002 |
| 333.15 | 600.00 | 0.0001 |
| 333.15 | 10000.00 | 0.0001 |
| 333.15 | 20000.00 | 0.0002 |
| 333.15 | 30000.00 | 0.0002 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Fluid (supercritical or subcritical phases) | Pressure, kPa - Fluid (supercritical or subcritical phases) | Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
| 360.00 | 200000.00 | 676.57 |
| 360.00 | 180000.00 | 668.57 |
| 360.00 | 160000.00 | 659.24 |
| 360.00 | 140000.00 | 649.66 |
| 360.00 | 120000.00 | 638.57 |
| 360.00 | 100000.00 | 626.29 |
| 360.00 | 90000.00 | 619.58 |
| 360.00 | 80000.00 | 612.02 |
| 360.00 | 70000.00 | 604.19 |
| 360.00 | 60000.00 | 595.41 |
| 360.00 | 50000.00 | 585.47 |
| 400.00 | 200000.00 | 658.6 |
| 400.00 | 180000.00 | 649.69 |
| 400.00 | 160000.00 | 639.75 |
| 400.00 | 140000.00 | 629.05 |
| 400.00 | 120000.00 | 617.0 |
| 400.00 | 100000.00 | 603.28 |
| 400.00 | 90000.00 | 595.58 |
| 400.00 | 80000.00 | 587.28 |
| 400.00 | 70000.00 | 578.11 |
| 400.00 | 60000.00 | 567.8 |
| 400.00 | 50000.00 | 556.11 |
| 440.00 | 200000.00 | 641.85 |
| 440.00 | 180000.00 | 632.12 |
| 440.00 | 160000.00 | 621.49 |
| 440.00 | 140000.00 | 609.84 |
| 440.00 | 120000.00 | 596.67 |
| 440.00 | 100000.00 | 581.43 |
| 440.00 | 90000.00 | 572.93 |
| 440.00 | 80000.00 | 563.51 |
| 440.00 | 70000.00 | 552.99 |
| 440.00 | 60000.00 | 541.19 |
| 440.00 | 50000.00 | 527.49 |
| 500.00 | 200000.00 | 617.68 |
| 500.00 | 180000.00 | 607.21 |
| 500.00 | 160000.00 | 595.57 |
| 500.00 | 140000.00 | 582.51 |
| 500.00 | 120000.00 | 567.64 |
| 500.00 | 100000.00 | 550.18 |
| 500.00 | 90000.00 | 540.26 |
| 500.00 | 80000.00 | 529.24 |
| 500.00 | 70000.00 | 517.01 |
| 500.00 | 60000.00 | 502.86 |
| 500.00 | 50000.00 | 485.76 |
| 550.00 | 200000.00 | 599.35 |
| 550.00 | 180000.00 | 588.11 |
| 550.00 | 160000.00 | 575.61 |
| 550.00 | 140000.00 | 561.8 |
| 550.00 | 120000.00 | 545.49 |
| 550.00 | 100000.00 | 526.47 |
| 550.00 | 90000.00 | 515.43 |
| 550.00 | 80000.00 | 503.05 |
| 550.00 | 70000.00 | 489.04 |
| 550.00 | 60000.00 | 472.65 |
| 550.00 | 50000.00 | 452.74 |
| 600.00 | 200000.00 | 582.23 |
| 600.00 | 180000.00 | 570.23 |
| 600.00 | 160000.00 | 556.81 |
| 600.00 | 140000.00 | 541.56 |
| 600.00 | 120000.00 | 524.18 |
| 600.00 | 100000.00 | 503.41 |
| 600.00 | 90000.00 | 491.53 |
| 600.00 | 80000.00 | 477.92 |
| 600.00 | 70000.00 | 462.25 |
| 600.00 | 60000.00 | 444.04 |
| 600.00 | 50000.00 | 421.67 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Fluid (supercritical or subcritical phases) | Pressure, kPa - Fluid (supercritical or subcritical phases) | Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
| 280.00 | 1000.00 | 595.47 |
| 280.00 | 2000.00 | 596.86 |
| 280.00 | 3000.00 | 598.22 |
| 280.00 | 5000.00 | 600.88 |
| 280.00 | 10000.00 | 607.05 |
| 280.00 | 20000.00 | 617.68 |
| 280.00 | 30000.00 | 626.91 |
| 280.00 | 40000.00 | 635.29 |
| 280.00 | 50000.00 | 642.77 |
| 280.00 | 60000.00 | 649.44 |
| 280.00 | 70000.00 | 655.79 |
| 280.00 | 80000.00 | 661.73 |
| 280.00 | 90000.00 | 667.23 |
| 280.00 | 100000.00 | 672.51 |
| 280.00 | 120000.00 | 682.08 |
| 280.00 | 140000.00 | 690.89 |
| 280.00 | 160000.00 | 698.82 |
| 280.00 | 180000.00 | 706.38 |
| 280.00 | 200000.00 | 713.34 |
| 300.00 | 1000.00 | 572.94 |
| 300.00 | 2000.00 | 574.58 |
| 300.00 | 3000.00 | 576.27 |
| 300.00 | 5000.00 | 579.56 |
| 300.00 | 10000.00 | 586.77 |
| 300.00 | 20000.00 | 599.44 |
| 300.00 | 30000.00 | 610.13 |
| 300.00 | 40000.00 | 619.89 |
| 300.00 | 50000.00 | 628.14 |
| 300.00 | 60000.00 | 635.82 |
| 300.00 | 70000.00 | 642.36 |
| 300.00 | 80000.00 | 648.71 |
| 300.00 | 90000.00 | 654.83 |
| 300.00 | 100000.00 | 660.41 |
| 300.00 | 120000.00 | 670.68 |
| 300.00 | 140000.00 | 680.05 |
| 300.00 | 160000.00 | 688.48 |
| 300.00 | 180000.00 | 696.25 |
| 300.00 | 200000.00 | 703.51 |
| 320.00 | 1000.00 | 548.24 |
| 320.00 | 2000.00 | 550.53 |
| 320.00 | 3000.00 | 552.73 |
| 320.00 | 5000.00 | 556.84 |
| 320.00 | 10000.00 | 566.09 |
| 320.00 | 20000.00 | 580.87 |
| 320.00 | 30000.00 | 593.19 |
| 320.00 | 40000.00 | 603.68 |
| 320.00 | 50000.00 | 612.97 |
| 320.00 | 60000.00 | 621.23 |
| 320.00 | 70000.00 | 628.85 |
| 320.00 | 80000.00 | 635.85 |
| 320.00 | 90000.00 | 642.47 |
| 320.00 | 100000.00 | 648.38 |
| 320.00 | 120000.00 | 659.38 |
| 320.00 | 140000.00 | 669.21 |
| 320.00 | 160000.00 | 678.31 |
| 320.00 | 180000.00 | 686.49 |
| 320.00 | 200000.00 | 694.12 |
| 340.00 | 1000.00 | 521.26 |
| 340.00 | 2000.00 | 524.21 |
| 340.00 | 3000.00 | 527.06 |
| 340.00 | 5000.00 | 532.46 |
| 340.00 | 10000.00 | 544.06 |
| 340.00 | 20000.00 | 561.99 |
| 340.00 | 30000.00 | 576.2 |
| 340.00 | 40000.00 | 588.27 |
| 340.00 | 50000.00 | 598.47 |
| 340.00 | 60000.00 | 607.64 |
| 340.00 | 70000.00 | 615.81 |
| 340.00 | 80000.00 | 623.32 |
| 340.00 | 90000.00 | 630.37 |
| 340.00 | 100000.00 | 636.58 |
| 340.00 | 120000.00 | 648.45 |
| 340.00 | 140000.00 | 658.64 |
| 340.00 | 160000.00 | 668.16 |
| 340.00 | 180000.00 | 676.9 |
| 340.00 | 200000.00 | 684.85 |
| 360.00 | 2000.00 | 494.28 |
| 360.00 | 3000.00 | 498.49 |
| 360.00 | 5000.00 | 505.91 |
| 360.00 | 10000.00 | 520.98 |
| 360.00 | 20000.00 | 542.91 |
| 360.00 | 30000.00 | 559.24 |
| 360.00 | 40000.00 | 572.58 |
| 360.00 | 50000.00 | 584.17 |
| 360.00 | 60000.00 | 593.9 |
| 360.00 | 70000.00 | 602.93 |
| 360.00 | 80000.00 | 610.9 |
| 360.00 | 90000.00 | 618.47 |
| 360.00 | 100000.00 | 625.39 |
| 360.00 | 120000.00 | 637.62 |
| 360.00 | 140000.00 | 648.76 |
| 360.00 | 160000.00 | 658.47 |
| 360.00 | 180000.00 | 667.68 |
| 360.00 | 200000.00 | 676.03 |
| 380.00 | 2000.00 | 456.63 |
| 380.00 | 3000.00 | 463.53 |
| 380.00 | 5000.00 | 474.94 |
| 380.00 | 10000.00 | 495.21 |
| 380.00 | 20000.00 | 522.42 |
| 380.00 | 30000.00 | 541.49 |
| 380.00 | 40000.00 | 556.53 |
| 380.00 | 50000.00 | 569.05 |
| 380.00 | 60000.00 | 580.01 |
| 380.00 | 70000.00 | 589.59 |
| 380.00 | 80000.00 | 598.34 |
| 380.00 | 90000.00 | 606.19 |
| 380.00 | 100000.00 | 613.44 |
| 380.00 | 120000.00 | 626.58 |
| 380.00 | 140000.00 | 638.25 |
| 380.00 | 160000.00 | 648.59 |
| 380.00 | 180000.00 | 658.14 |
| 380.00 | 200000.00 | 666.86 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 3000.00 | 380.00 | 463.27 |
| 5000.00 | 380.00 | 474.65 |
| 5000.00 | 400.00 | 437.19 |
| 10000.00 | 380.00 | 494.93 |
| 10000.00 | 400.00 | 466.97 |
| 10000.00 | 420.00 | 436.16 |
| 10000.00 | 440.00 | 401.28 |
| 20000.00 | 380.00 | 521.9 |
| 20000.00 | 400.00 | 500.93 |
| 20000.00 | 420.00 | 479.15 |
| 20000.00 | 440.00 | 457.43 |
| 30000.00 | 400.00 | 522.83 |
| 30000.00 | 420.00 | 504.89 |
| 30000.00 | 440.00 | 487.23 |
| 40000.00 | 380.00 | 555.85 |
| 40000.00 | 400.00 | 539.73 |
| 40000.00 | 420.00 | 523.9 |
| 40000.00 | 440.00 | 508.57 |
| 50000.00 | 400.00 | 553.54 |
| 50000.00 | 420.00 | 539.08 |
| 50000.00 | 440.00 | 525.26 |
| 60000.00 | 380.00 | 579.32 |
| 60000.00 | 400.00 | 565.44 |
| 60000.00 | 420.00 | 551.8 |
| 60000.00 | 440.00 | 539.13 |
| 70000.00 | 400.00 | 575.77 |
| 70000.00 | 420.00 | 563.07 |
| 70000.00 | 440.00 | 551.03 |
| 80000.00 | 380.00 | 597.57 |
| 80000.00 | 400.00 | 585.08 |
| 80000.00 | 420.00 | 572.94 |
| 80000.00 | 440.00 | 561.56 |
| 90000.00 | 400.00 | 593.33 |
| 90000.00 | 420.00 | 581.86 |
| 90000.00 | 440.00 | 571.14 |
| 100000.00 | 380.00 | 612.79 |
| 100000.00 | 400.00 | 601.18 |
| 100000.00 | 420.00 | 589.89 |
| 100000.00 | 440.00 | 579.66 |
| 120000.00 | 380.00 | 625.93 |
| 120000.00 | 400.00 | 614.9 |
| 120000.00 | 420.00 | 604.27 |
| 120000.00 | 440.00 | 594.85 |
| 140000.00 | 380.00 | 637.29 |
| 140000.00 | 400.00 | 627.05 |
| 140000.00 | 420.00 | 617.11 |
| 140000.00 | 440.00 | 608.04 |
| 160000.00 | 380.00 | 647.82 |
| 160000.00 | 400.00 | 637.77 |
| 160000.00 | 420.00 | 628.25 |
| 160000.00 | 440.00 | 619.73 |
| 180000.00 | 380.00 | 657.28 |
| 180000.00 | 400.00 | 647.6 |
| 180000.00 | 420.00 | 638.65 |
| 180000.00 | 440.00 | 630.34 |
| 200000.00 | 380.00 | 665.98 |
| 200000.00 | 400.00 | 656.49 |
| 200000.00 | 420.00 | 647.73 |
| 200000.00 | 440.00 | 639.98 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Fluid (supercritical or subcritical phases) | Pressure, kPa - Fluid (supercritical or subcritical phases) | Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
| 298.12 | 221.39 | 5.5728 |
| 298.12 | 221.35 | 5.5716 |
| 298.14 | 196.75 | 4.9091 |
| 298.14 | 196.77 | 4.9096 |
| 298.14 | 175.29 | 4.3414 |
| 298.14 | 175.29 | 4.3415 |
| 298.11 | 162.81 | 4.0157 |
| 298.11 | 162.82 | 4.016 |
| 298.12 | 142.16 | 3.4823 |
| 298.13 | 142.17 | 3.4826 |
| 298.13 | 123.43 | 3.0049 |
| 298.13 | 123.44 | 3.0052 |
| 298.14 | 102.90 | 2.4887 |
| 298.14 | 102.91 | 2.4889 |
| 298.14 | 82.37 | 1.9794 |
| 298.14 | 82.38 | 1.9797 |
| 298.14 | 61.79 | 1.4756 |
| 298.14 | 61.80 | 1.4758 |
| 298.15 | 57.18 | 1.3635 |
| 298.15 | 57.18 | 1.3636 |
| 322.98 | 450.39 | 11.024 |
| 323.00 | 450.69 | 11.032 |
| 323.01 | 450.89 | 11.037 |
| 323.06 | 392.10 | 9.426 |
| 323.08 | 392.50 | 9.4391 |
| 323.09 | 392.90 | 9.4492 |
| 323.11 | 380.78 | 9.1236 |
| 323.11 | 380.74 | 9.1236 |
| 323.12 | 380.76 | 9.1272 |
| 323.12 | 330.12 | 7.8092 |
| 323.12 | 330.36 | 7.8164 |
| 323.13 | 330.63 | 7.8215 |
| 323.13 | 301.54 | 7.0807 |
| 323.13 | 303.39 | 7.1241 |
| 323.13 | 305.32 | 7.1762 |
| 323.13 | 261.18 | 6.0223 |
| 323.13 | 261.21 | 6.023 |
| 323.14 | 261.28 | 6.0252 |
| 323.14 | 215.87 | 4.9169 |
| 323.14 | 215.65 | 4.9111 |
| 323.14 | 215.63 | 4.9096 |
| 323.14 | 184.24 | 4.1645 |
| 323.15 | 184.35 | 4.1652 |
| 323.15 | 184.36 | 4.1667 |
| 323.15 | 150.03 | 3.3622 |
| 323.15 | 150.04 | 3.3622 |
| 323.14 | 132.43 | 2.9506 |
| 323.14 | 132.44 | 2.9492 |
| 323.14 | 132.46 | 2.9499 |
| 323.14 | 112.93 | 2.5057 |
| 323.14 | 112.94 | 2.5035 |
| 323.14 | 112.96 | 2.5057 |
| 323.14 | 90.51 | 1.9979 |
| 323.14 | 90.52 | 1.9986 |
| 323.14 | 66.38 | 1.4575 |
| 323.14 | 66.38 | 1.4567 |
| 323.14 | 66.39 | 1.4553 |
| 323.14 | 58.20 | 1.2744 |
| 323.14 | 58.20 | 1.2766 |
| 323.14 | 58.21 | 1.2766 |
| 348.03 | 813.99 | 19.581 |
| 348.03 | 814.13 | 19.586 |
| 348.03 | 813.85 | 19.576 |
| 348.13 | 760.25 | 17.999 |
| 348.13 | 760.34 | 18.002 |
| 348.12 | 677.52 | 15.682 |
| 348.12 | 677.82 | 15.691 |
| 348.14 | 618.24 | 14.097 |
| 348.14 | 618.34 | 14.099 |
| 348.15 | 516.76 | 11.497 |
| 348.15 | 516.69 | 11.497 |
| 348.15 | 454.98 | 9.9811 |
| 348.15 | 455.21 | 9.9833 |
| 348.15 | 340.91 | 7.3031 |
| 348.15 | 338.38 | 7.2445 |
| 348.15 | 337.86 | 7.2315 |
| 348.15 | 337.88 | 7.2315 |
| 348.14 | 293.19 | 6.2173 |
| 348.14 | 293.73 | 6.2296 |
| 348.14 | 93.82 | 1.9124 |
| 348.14 | 93.83 | 1.9131 |
| 348.15 | 63.28 | 1.2845 |
| 348.15 | 63.30 | 1.286 |
| 373.15 | 1366.40 | 33.46 |
| 373.15 | 1367.10 | 33.484 |
| 373.14 | 1262.70 | 30.019 |
| 373.14 | 1263.00 | 30.031 |
| 373.14 | 1095.40 | 24.953 |
| 373.14 | 1095.50 | 24.958 |
| 373.13 | 916.45 | 20.053 |
| 373.13 | 916.45 | 20.052 |
| 373.14 | 838.34 | 18.049 |
| 373.15 | 750.55 | 15.881 |
| 373.14 | 751.04 | 15.893 |
| 373.14 | 669.81 | 13.955 |
| 373.14 | 670.00 | 13.959 |
| 373.14 | 572.54 | 11.724 |
| 373.14 | 572.60 | 11.728 |
| 373.14 | 493.81 | 9.9744 |
| 373.14 | 493.67 | 9.9707 |
| 373.15 | 439.63 | 8.8018 |
| 373.15 | 441.23 | 8.8343 |
| 373.15 | 392.71 | 7.8028 |
| 373.15 | 344.33 | 6.7909 |
| 373.15 | 344.35 | 6.7909 |
| 373.14 | 273.38 | 5.3326 |
| 373.14 | 274.72 | 5.3593 |
| 373.15 | 210.37 | 4.0602 |
| 373.14 | 210.39 | 4.0609 |
| 373.14 | 157.75 | 3.0215 |
| 373.13 | 157.77 | 3.0215 |
| 373.13 | 106.93 | 2.0348 |
| 373.13 | 106.95 | 2.0363 |
| 373.13 | 106.98 | 2.037 |
| 373.14 | 57.69 | 1.0901 |
| 373.14 | 57.72 | 1.0901 |
| 373.14 | 57.76 | 1.0909 |
| 423.48 | 3280.80 | 96.642 |
| 423.47 | 3280.90 | 96.663 |
| 424.21 | 3176.80 | 88.401 |
| 424.21 | 3177.00 | 88.415 |
| 423.28 | 3171.40 | 89.266 |
| 423.20 | 3170.20 | 89.28 |
| 423.19 | 3006.00 | 79.774 |
| 423.20 | 3005.80 | 79.773 |
| 423.20 | 2781.60 | 69.058 |
| 423.20 | 2781.10 | 69.059 |
| 423.11 | 2532.50 | 59.203 |
| 423.12 | 2534.00 | 59.251 |
| 423.13 | 2535.60 | 59.303 |
| 423.17 | 2272.30 | 50.31 |
| 423.17 | 1490.20 | 29.071 |
| 423.19 | 1490.00 | 29.063 |
| 423.24 | 1016.10 | 18.65 |
| 423.25 | 1015.90 | 18.648 |
| 423.26 | 884.12 | 15.981 |
| 423.26 | 884.38 | 15.987 |
| 423.20 | 653.48 | 11.519 |
| 423.19 | 654.26 | 11.533 |
| 423.17 | 452.37 | 7.8076 |
| 423.17 | 450.91 | 7.7808 |
| 423.16 | 195.54 | 3.2893 |
| 423.16 | 195.59 | 3.2893 |
| 428.14 | 30023.00 | 498.21 |
| 428.14 | 30022.00 | 498.2 |
| 428.14 | 30018.00 | 498.2 |
| 428.21 | 22974.00 | 480.02 |
| 428.21 | 22974.00 | 480.02 |
| 428.20 | 22973.00 | 480.02 |
| 428.15 | 17077.00 | 460.12 |
| 428.15 | 17075.00 | 460.12 |
| 428.15 | 12773.00 | 440.28 |
| 428.16 | 12732.00 | 440.05 |
| 428.16 | 12735.00 | 440.06 |
| 428.16 | 9661.10 | 420.21 |
| 428.16 | 9662.30 | 420.22 |
| 428.17 | 7466.20 | 399.67 |
| 428.16 | 7467.10 | 399.68 |
| 428.16 | 7467.50 | 399.69 |
| 428.13 | 5948.90 | 378.0 |
| 428.13 | 5949.60 | 378.01 |
| 428.13 | 5949.60 | 378.02 |
| 428.09 | 5150.20 | 360.25 |
| 428.09 | 5149.90 | 360.26 |
| 428.10 | 4625.90 | 341.66 |
| 428.11 | 4626.60 | 341.66 |
| 428.11 | 4626.80 | 341.65 |
| 428.18 | 4312.00 | 322.22 |
| 428.18 | 4312.40 | 322.24 |
| 428.18 | 4312.40 | 322.25 |
| 428.14 | 4145.90 | 304.6 |
| 428.14 | 4146.20 | 304.61 |
| 428.15 | 4067.30 | 289.0 |
| 428.15 | 4067.50 | 288.98 |
| 428.20 | 4030.00 | 274.89 |
| 428.20 | 4030.10 | 274.9 |
| 428.13 | 3990.10 | 251.58 |
| 428.13 | 3990.10 | 251.63 |
| 428.12 | 3984.80 | 246.5 |
| 428.12 | 3984.90 | 246.49 |
| 428.18 | 3976.30 | 230.48 |
| 428.17 | 3976.10 | 230.45 |
| 428.12 | 3964.90 | 218.37 |
| 428.13 | 3964.80 | 218.33 |
| 428.19 | 3953.50 | 199.12 |
| 428.18 | 3953.30 | 199.18 |
| 428.19 | 3938.70 | 185.24 |
| 428.19 | 3939.20 | 185.3 |
| 428.19 | 3884.10 | 159.21 |
| 428.19 | 3883.80 | 159.22 |
| 428.34 | 3805.10 | 138.83 |
| 428.39 | 3806.50 | 138.8 |
| 428.20 | 3793.80 | 137.58 |
| 428.18 | 3790.90 | 137.62 |
| 428.13 | 3655.20 | 119.22 |
| 428.14 | 3655.70 | 119.23 |
| 428.14 | 3427.10 | 99.322 |
| 428.15 | 3427.20 | 99.316 |
| 428.16 | 3263.80 | 88.856 |
| 428.15 | 3263.70 | 88.854 |
| 428.23 | 3108.60 | 80.486 |
| 428.22 | 3107.80 | 80.455 |
| 428.14 | 2862.80 | 69.471 |
| 428.13 | 2862.90 | 69.476 |
| 428.13 | 2624.70 | 60.36 |
| 428.13 | 2624.60 | 60.353 |
| 428.12 | 2306.20 | 49.889 |
| 428.12 | 2306.20 | 49.887 |
| 428.10 | 1964.10 | 40.163 |
| 428.11 | 1964.30 | 40.167 |
| 428.21 | 1539.80 | 29.634 |
| 428.21 | 1540.10 | 29.642 |
| 428.18 | 1098.50 | 20.025 |
| 428.18 | 1099.10 | 20.038 |
| 428.15 | 1040.70 | 18.847 |
| 428.14 | 1041.20 | 18.856 |
| 428.11 | 904.86 | 16.141 |
| 428.10 | 904.90 | 16.138 |
| 428.10 | 796.14 | 14.038 |
| 428.10 | 796.19 | 14.041 |
| 428.12 | 685.03 | 11.939 |
| 428.13 | 684.54 | 11.929 |
| 428.13 | 578.67 | 9.9774 |
| 428.14 | 578.76 | 9.9803 |
| 428.13 | 480.91 | 8.2126 |
| 428.14 | 480.81 | 8.2112 |
| 428.09 | 194.34 | 3.2308 |
| 428.08 | 194.36 | 3.2322 |
| 428.11 | 131.61 | 2.1741 |
| 428.11 | 131.64 | 2.1741 |
| 428.18 | 62.10 | 1.0176 |
| 428.17 | 62.10 | 1.0183 |
| 428.16 | 62.10 | 1.0176 |
| 448.15 | 29472.00 | 478.91 |
| 448.14 | 29460.00 | 478.91 |
| 448.17 | 23154.00 | 460.09 |
| 448.16 | 23152.00 | 460.08 |
| 448.14 | 18184.00 | 440.74 |
| 448.14 | 18187.00 | 440.74 |
| 448.15 | 14319.00 | 420.46 |
| 448.17 | 14321.00 | 420.46 |
| 448.15 | 11528.00 | 400.23 |
| 448.15 | 11529.00 | 400.23 |
| 448.17 | 9538.60 | 380.13 |
| 448.17 | 9537.40 | 380.12 |
| 448.16 | 8140.60 | 359.99 |
| 448.16 | 8139.40 | 359.98 |
| 448.14 | 7191.00 | 340.37 |
| 448.13 | 7189.80 | 340.36 |
| 448.16 | 6551.40 | 321.12 |
| 448.16 | 6551.10 | 321.12 |
| 448.11 | 6144.80 | 304.18 |
| 448.11 | 6145.00 | 304.17 |
| 448.28 | 5785.10 | 281.66 |
| 448.27 | 5784.60 | 281.65 |
| 448.15 | 5551.90 | 263.05 |
| 448.15 | 5553.70 | 263.02 |
| 448.18 | 5346.70 | 240.34 |
| 448.17 | 5346.60 | 240.34 |
| 448.13 | 5203.20 | 222.02 |
| 448.13 | 5203.50 | 222.03 |
| 448.11 | 5054.80 | 201.47 |
| 448.11 | 5054.50 | 201.47 |
| 448.09 | 4846.20 | 174.16 |
| 448.13 | 4847.00 | 174.1 |
| 448.23 | 4727.10 | 160.07 |
| 448.23 | 4727.00 | 160.07 |
| 448.17 | 4498.30 | 138.72 |
| 448.18 | 4498.10 | 138.68 |
| 448.13 | 4161.60 | 114.81 |
| 448.13 | 4161.60 | 114.81 |
| 448.18 | 3747.80 | 92.905 |
| 448.19 | 3747.90 | 92.91 |
| 448.18 | 3433.90 | 79.739 |
| 448.18 | 3433.70 | 79.735 |
| 448.15 | 3073.30 | 66.943 |
| 448.16 | 3073.30 | 66.941 |
| 448.16 | 2511.80 | 50.321 |
| 448.16 | 2512.10 | 50.329 |
| 448.17 | 2073.00 | 39.287 |
| 448.16 | 2073.70 | 39.305 |
| 448.16 | 1662.20 | 30.086 |
| 448.15 | 1661.90 | 30.078 |
| 448.17 | 1158.40 | 19.932 |
| 448.17 | 1158.40 | 19.932 |
| 448.16 | 807.76 | 13.456 |
| 448.15 | 807.60 | 13.453 |
| 448.15 | 618.60 | 10.141 |
| 448.15 | 618.43 | 10.135 |
| 448.16 | 508.50 | 8.2591 |
| 448.16 | 509.69 | 8.28 |
| 448.16 | 430.17 | 6.9362 |
| 448.16 | 431.02 | 6.95 |
| 448.15 | 220.17 | 3.4915 |
| 448.16 | 220.38 | 3.4965 |
| Reference | ||
Speed of sound, m/s
Operational condition: Frequency, MHz = 8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 200.00 | 1101.43 | 1447.79 |
| 200.00 | 2102.08 | 1453.53 |
| 200.00 | 3102.76 | 1459.25 |
| 200.00 | 4103.47 | 1464.89 |
| 200.00 | 5104.18 | 1470.49 |
| 200.00 | 6105.13 | 1476.03 |
| 200.00 | 7105.88 | 1481.53 |
| 200.00 | 8106.60 | 1486.99 |
| 200.00 | 9107.34 | 1492.39 |
| 200.00 | 10108.00 | 1497.75 |
| 200.00 | 12609.80 | 1510.92 |
| 200.00 | 15111.60 | 1523.84 |
| 200.00 | 17613.40 | 1536.5 |
| 200.00 | 20115.20 | 1548.92 |
| 200.00 | 25118.80 | 1573.08 |
| 200.00 | 30122.60 | 1596.41 |
| 200.00 | 35126.20 | 1618.97 |
| 199.99 | 40128.50 | 1640.8 |
| 199.99 | 45132.10 | 1662.03 |
| 199.99 | 50135.60 | 1682.63 |
| 200.00 | 60142.70 | 1722.21 |
| 200.00 | 70149.80 | 1759.84 |
| 200.00 | 80156.90 | 1795.79 |
| 200.00 | 90164.00 | 1830.15 |
| 200.00 | 100171.00 | 1863.22 |
| 201.00 | 250.62 | 1437.19 |
| 201.00 | 600.55 | 1439.24 |
| 201.00 | 1100.47 | 1442.14 |
| 201.00 | 1101.45 | 1442.16 |
| 201.00 | 2101.94 | 1447.96 |
| 201.00 | 2102.01 | 1447.96 |
| 201.00 | 3102.62 | 1453.68 |
| 201.00 | 4103.38 | 1459.38 |
| 201.00 | 5104.04 | 1465.01 |
| 220.00 | 249.98 | 1330.46 |
| 220.00 | 599.68 | 1332.78 |
| 220.00 | 1100.72 | 1336.09 |
| 220.00 | 1100.82 | 1336.09 |
| 220.00 | 10107.00 | 1392.58 |
| 220.00 | 12608.80 | 1407.34 |
| 220.00 | 15110.60 | 1421.75 |
| 220.00 | 17612.40 | 1435.83 |
| 220.00 | 2101.56 | 1342.65 |
| 220.00 | 2101.82 | 1342.65 |
| 220.00 | 2102.10 | 1342.65 |
| 220.00 | 2103.43 | 1342.64 |
| 220.00 | 3102.31 | 1349.14 |
| 220.00 | 3104.10 | 1349.13 |
| 220.00 | 4103.01 | 1355.55 |
| 220.00 | 4104.72 | 1355.54 |
| 220.00 | 5103.60 | 1361.88 |
| 220.00 | 6104.22 | 1368.15 |
| 220.00 | 7104.87 | 1374.34 |
| 220.00 | 8105.49 | 1380.51 |
| 220.00 | 9106.16 | 1386.56 |
| 220.00 | 20114.20 | 1449.59 |
| 220.00 | 25117.70 | 1476.25 |
| 220.00 | 30121.30 | 1501.85 |
| 220.00 | 35124.90 | 1526.52 |
| 220.00 | 40129.10 | 1550.28 |
| 220.00 | 45132.70 | 1573.31 |
| 220.00 | 50136.40 | 1595.59 |
| 220.00 | 60143.60 | 1638.17 |
| 220.00 | 70150.80 | 1678.49 |
| 220.00 | 80157.90 | 1716.78 |
| 220.00 | 90165.10 | 1753.24 |
| 220.00 | 100172.00 | 1788.2 |
| 240.00 | 252.21 | 1219.33 |
| 240.00 | 602.15 | 1222.0 |
| 240.00 | 1103.02 | 1225.8 |
| 240.00 | 2103.48 | 1233.3 |
| 240.00 | 2104.31 | 1233.3 |
| 240.00 | 3104.05 | 1240.7 |
| 240.00 | 3105.10 | 1240.7 |
| 240.00 | 4104.68 | 1248.0 |
| 240.00 | 4105.89 | 1248.0 |
| 240.00 | 5105.31 | 1255.2 |
| 240.00 | 5106.62 | 1255.2 |
| 240.00 | 6107.33 | 1262.31 |
| 240.00 | 12612.00 | 1306.37 |
| 240.00 | 15113.00 | 1322.45 |
| 240.00 | 17614.70 | 1338.08 |
| 240.00 | 20116.40 | 1353.31 |
| 240.00 | 25119.90 | 1382.68 |
| 240.00 | 30123.40 | 1410.72 |
| 240.00 | 35126.80 | 1437.56 |
| 240.00 | 40130.30 | 1463.36 |
| 240.00 | 45134.10 | 1488.2 |
| 240.00 | 50137.60 | 1512.19 |
| 240.00 | 60144.60 | 1557.82 |
| 240.00 | 70151.60 | 1600.75 |
| 240.00 | 7108.05 | 1269.32 |
| 240.00 | 8108.78 | 1276.24 |
| 240.00 | 9109.52 | 1283.08 |
| 240.00 | 10110.20 | 1289.84 |
| 240.00 | 80158.50 | 1641.41 |
| 240.00 | 90165.30 | 1680.02 |
| 240.00 | 100172.00 | 1716.86 |
| 260.00 | 251.45 | 1109.14 |
| 260.00 | 601.45 | 1112.23 |
| 260.00 | 1102.15 | 1116.62 |
| 260.00 | 2102.77 | 1125.27 |
| 260.00 | 2103.13 | 1125.31 |
| 260.00 | 3103.43 | 1133.77 |
| 260.00 | 3103.82 | 1133.82 |
| 260.00 | 4104.07 | 1142.13 |
| 260.00 | 4104.51 | 1142.17 |
| 260.00 | 5104.72 | 1150.34 |
| 260.00 | 5105.21 | 1150.38 |
| 260.00 | 6105.88 | 1158.47 |
| 260.00 | 7106.52 | 1166.42 |
| 260.00 | 8107.23 | 1174.26 |
| 260.00 | 9107.95 | 1181.97 |
| 260.00 | 10108.30 | 1189.58 |
| 259.99 | 12610.00 | 1208.12 |
| 260.00 | 15111.70 | 1226.05 |
| 260.00 | 17613.40 | 1243.41 |
| 260.00 | 20115.10 | 1260.26 |
| 260.00 | 25118.60 | 1292.53 |
| 260.00 | 30122.10 | 1323.15 |
| 260.00 | 35125.50 | 1352.3 |
| 260.00 | 40129.00 | 1380.18 |
| 260.00 | 45132.70 | 1406.9 |
| 260.00 | 50136.40 | 1432.6 |
| 260.00 | 60143.60 | 1481.28 |
| 260.00 | 70150.70 | 1526.84 |
| 259.99 | 80157.60 | 1569.77 |
| 259.99 | 90164.60 | 1610.4 |
| 260.00 | 100172.00 | 1649.05 |
| 280.00 | 250.96 | 999.47 |
| 280.00 | 601.00 | 1003.08 |
| 280.00 | 1101.74 | 1008.21 |
| 280.00 | 2102.38 | 1018.28 |
| 280.00 | 12609.90 | 1112.63 |
| 280.00 | 15111.50 | 1132.65 |
| 280.00 | 17613.30 | 1151.93 |
| 280.00 | 20114.90 | 1170.54 |
| 280.00 | 2102.38 | 1018.3 |
| 280.00 | 3103.03 | 1028.13 |
| 280.00 | 3103.12 | 1028.15 |
| 280.00 | 4103.63 | 1037.77 |
| 280.00 | 4103.90 | 1037.79 |
| 280.00 | 5104.07 | 1047.2 |
| 280.00 | 5104.65 | 1047.23 |
| 280.00 | 6105.39 | 1056.49 |
| 280.00 | 7106.09 | 1065.56 |
| 280.00 | 8106.82 | 1074.46 |
| 280.00 | 9107.55 | 1083.21 |
| 280.00 | 10108.20 | 1091.8 |
| 280.00 | 25118.30 | 1205.97 |
| 280.00 | 30121.70 | 1239.32 |
| 280.00 | 35125.10 | 1270.88 |
| 280.00 | 40128.50 | 1300.89 |
| 280.00 | 45132.00 | 1329.54 |
| 280.00 | 50135.30 | 1356.98 |
| 280.00 | 60142.30 | 1408.68 |
| 280.00 | 70149.30 | 1456.81 |
| 280.00 | 80158.90 | 1501.97 |
| 280.00 | 90165.90 | 1544.56 |
| 280.00 | 100173.00 | 1584.94 |
| 300.00 | 599.94 | 893.833 |
| 300.01 | 1100.40 | 899.926 |
| 300.00 | 2102.01 | 911.889 |
| 300.00 | 2104.25 | 911.909 |
| 300.00 | 3102.80 | 923.459 |
| 300.00 | 3104.95 | 923.478 |
| 300.00 | 4103.65 | 934.713 |
| 300.00 | 4105.67 | 934.728 |
| 300.00 | 5104.44 | 945.669 |
| 300.00 | 5105.89 | 945.676 |
| 300.00 | 6106.51 | 956.354 |
| 300.00 | 7107.18 | 966.776 |
| 300.00 | 8107.81 | 976.954 |
| 300.00 | 12610.50 | 1020.17 |
| 300.00 | 15112.20 | 1042.56 |
| 300.00 | 17613.90 | 1063.97 |
| 300.00 | 20115.00 | 1084.5 |
| 300.00 | 25118.50 | 1123.32 |
| 300.00 | 30121.90 | 1159.56 |
| 300.00 | 35125.40 | 1193.62 |
| 300.00 | 40128.90 | 1225.82 |
| 300.00 | 45132.40 | 1256.41 |
| 300.00 | 50135.90 | 1285.58 |
| 300.00 | 60143.00 | 1340.29 |
| 300.00 | 70150.10 | 1390.94 |
| 299.99 | 80158.10 | 1438.22 |
| 300.00 | 9108.38 | 986.906 |
| 300.00 | 10108.80 | 996.678 |
| 299.99 | 90165.20 | 1482.66 |
| 299.99 | 100172.00 | 1524.68 |
| 320.00 | 601.27 | 783.221 |
| 320.00 | 1101.18 | 790.665 |
| 320.00 | 2101.87 | 805.078 |
| 320.00 | 2104.08 | 805.159 |
| 320.00 | 3102.51 | 818.927 |
| 320.00 | 3104.80 | 819.008 |
| 320.00 | 4103.20 | 832.273 |
| 320.00 | 4105.51 | 832.354 |
| 320.00 | 5103.84 | 845.165 |
| 320.00 | 5106.14 | 845.242 |
| 320.00 | 6106.80 | 857.711 |
| 320.00 | 7107.48 | 869.802 |
| 320.00 | 8108.17 | 881.54 |
| 320.00 | 9108.89 | 892.953 |
| 320.00 | 10109.10 | 904.045 |
| 320.00 | 10109.60 | 904.067 |
| 320.00 | 12611.30 | 930.654 |
| 320.00 | 15112.90 | 955.743 |
| 320.00 | 17614.70 | 979.543 |
| 320.00 | 20116.40 | 1002.21 |
| 320.00 | 25119.90 | 1044.68 |
| 320.00 | 30123.40 | 1083.95 |
| 320.00 | 35126.90 | 1120.58 |
| 320.00 | 40130.40 | 1155.01 |
| 320.00 | 45134.00 | 1187.55 |
| 320.00 | 50137.30 | 1218.44 |
| 320.00 | 50137.50 | 1218.44 |
| 320.00 | 60144.40 | 1276.1 |
| 320.00 | 70151.60 | 1329.16 |
| 320.00 | 80158.40 | 1378.48 |
| 320.00 | 90165.50 | 1424.69 |
| 320.00 | 100173.00 | 1468.23 |
| 340.00 | 1100.43 | 678.122 |
| 340.00 | 2101.09 | 696.215 |
| 340.00 | 2103.65 | 696.271 |
| 340.00 | 3101.74 | 713.3 |
| 340.00 | 3104.31 | 713.359 |
| 340.00 | 4102.42 | 729.532 |
| 340.00 | 4105.01 | 729.589 |
| 340.00 | 5102.92 | 745.009 |
| 340.00 | 5105.58 | 745.066 |
| 340.00 | 6106.20 | 759.882 |
| 340.00 | 7106.82 | 774.104 |
| 340.00 | 8107.47 | 787.795 |
| 340.00 | 9108.12 | 801.008 |
| 340.00 | 10106.50 | 813.726 |
| 340.00 | 10108.50 | 813.773 |
| 340.00 | 12610.40 | 844.028 |
| 340.00 | 15112.20 | 872.222 |
| 340.00 | 17614.00 | 898.696 |
| 340.00 | 20115.70 | 923.702 |
| 340.00 | 25119.20 | 970.085 |
| 340.00 | 30122.60 | 1012.52 |
| 340.00 | 35126.10 | 1051.8 |
| 340.00 | 40129.60 | 1088.46 |
| 340.00 | 45133.00 | 1122.94 |
| 340.00 | 50136.50 | 1155.53 |
| 340.00 | 60144.70 | 1216.04 |
| 340.00 | 70151.80 | 1271.43 |
| 340.00 | 80158.80 | 1322.7 |
| 340.00 | 90165.80 | 1370.55 |
| 340.00 | 100173.00 | 1415.54 |
| 360.00 | 2100.75 | 582.292 |
| 360.00 | 2103.86 | 582.372 |
| 360.00 | 3101.39 | 604.477 |
| 360.00 | 3101.42 | 604.479 |
| 360.00 | 3104.59 | 604.562 |
| 360.00 | 4102.00 | 625.0 |
| 360.00 | 4102.06 | 624.999 |
| 360.00 | 4105.35 | 625.09 |
| 360.00 | 5102.59 | 644.168 |
| 360.00 | 5102.98 | 644.182 |
| 360.00 | 5106.07 | 644.251 |
| 360.00 | 6106.86 | 662.279 |
| 360.00 | 7107.63 | 679.33 |
| 360.00 | 8108.38 | 695.538 |
| 360.00 | 9109.09 | 711.01 |
| 360.00 | 10109.80 | 725.827 |
| 360.00 | 12611.50 | 760.445 |
| 360.00 | 15113.30 | 792.205 |
| 360.00 | 17615.10 | 821.665 |
| 360.00 | 20116.80 | 849.226 |
| 360.00 | 25120.40 | 899.751 |
| 360.00 | 30124.20 | 945.466 |
| 360.00 | 35127.80 | 987.407 |
| 360.00 | 40131.20 | 1026.3 |
| 360.00 | 45134.60 | 1062.68 |
| 360.00 | 50138.10 | 1096.92 |
| 360.00 | 60145.10 | 1160.16 |
| 360.00 | 70152.10 | 1217.74 |
| 360.00 | 80159.00 | 1270.82 |
| 360.00 | 90166.10 | 1320.23 |
| 360.00 | 100173.00 | 1366.55 |
| 380.00 | 2103.23 | 456.129 |
| 380.00 | 3104.16 | 488.076 |
| 380.00 | 4105.03 | 515.932 |
| 380.00 | 5105.83 | 540.877 |
| 380.00 | 6106.71 | 563.618 |
| 380.00 | 7107.52 | 584.618 |
| 380.00 | 8108.31 | 604.199 |
| 380.00 | 9109.12 | 622.597 |
| 380.00 | 10109.90 | 639.978 |
| 380.00 | 12611.10 | 679.849 |
| 380.00 | 15112.80 | 715.711 |
| 380.00 | 17614.50 | 748.486 |
| 380.00 | 20116.20 | 778.799 |
| 380.00 | 25119.70 | 833.691 |
| 380.00 | 30123.30 | 882.725 |
| 380.00 | 35126.80 | 927.317 |
| 380.00 | 40131.60 | 968.4 |
| 380.00 | 45135.10 | 1006.62 |
| 380.00 | 50138.70 | 1042.44 |
| 380.00 | 60145.70 | 1108.27 |
| 380.00 | 70152.70 | 1167.91 |
| 380.00 | 80159.70 | 1222.69 |
| 380.00 | 90166.70 | 1273.52 |
| 380.00 | 100174.00 | 1321.06 |
| 400.00 | 2704.85 | 329.55 |
| 400.00 | 3105.08 | 351.68 |
| 400.00 | 4105.76 | 396.177 |
| 400.00 | 5106.37 | 431.84 |
| 400.00 | 6107.01 | 462.275 |
| 400.00 | 7107.72 | 489.164 |
| 400.00 | 8108.42 | 513.443 |
| 400.00 | 9109.39 | 535.712 |
| 400.00 | 10110.20 | 556.355 |
| 400.00 | 12612.00 | 602.563 |
| 400.00 | 15113.90 | 643.081 |
| 400.00 | 17615.70 | 679.473 |
| 400.00 | 20117.50 | 712.704 |
| 400.00 | 25121.10 | 772.062 |
| 400.00 | 30124.70 | 824.409 |
| 400.00 | 35128.30 | 871.587 |
| 400.00 | 40131.50 | 914.764 |
| 400.00 | 45135.00 | 954.727 |
| 400.00 | 50138.40 | 992.039 |
| 400.00 | 60145.30 | 1060.28 |
| 400.00 | 70152.30 | 1121.82 |
| 400.00 | 80159.20 | 1178.14 |
| 400.00 | 90166.10 | 1230.27 |
| 400.00 | 100173.00 | 1278.93 |
| 420.00 | 4104.41 | 244.514 |
| 420.00 | 4455.16 | 271.524 |
| 420.00 | 4604.99 | 281.85 |
| 420.00 | 4955.63 | 302.472 |
| 420.00 | 5105.08 | 310.479 |
| 420.00 | 5456.11 | 327.761 |
| 420.00 | 5605.74 | 334.633 |
| 420.00 | 6105.77 | 355.802 |
| 420.00 | 6606.48 | 374.829 |
| 420.00 | 7106.50 | 392.204 |
| 420.00 | 8107.22 | 423.269 |
| 420.00 | 9107.96 | 450.696 |
| 420.00 | 10109.00 | 475.453 |
| 420.00 | 12610.80 | 529.119 |
| 420.00 | 15112.50 | 574.769 |
| 420.00 | 17614.90 | 614.982 |
| 420.00 | 20116.70 | 651.2 |
| 420.00 | 25120.20 | 714.992 |
| 420.00 | 30123.70 | 770.535 |
| 420.00 | 35127.10 | 820.167 |
| 420.00 | 40130.60 | 865.305 |
| 420.00 | 45134.00 | 906.887 |
| 420.00 | 50137.50 | 945.566 |
| 420.00 | 50138.00 | 945.569 |
| 420.00 | 55141.50 | 981.829 |
| 420.00 | 60145.00 | 1016.01 |
| 420.00 | 70152.10 | 1079.28 |
| 420.00 | 80159.20 | 1137.01 |
| 420.00 | 90166.30 | 1190.31 |
| 420.00 | 100173.00 | 1239.96 |
| 430.00 | 5105.60 | 236.474 |
| 430.00 | 5355.26 | 258.169 |
| 430.00 | 5605.96 | 273.029 |
| 430.00 | 5855.60 | 287.251 |
| 430.00 | 6106.29 | 300.071 |
| 430.00 | 6356.29 | 311.899 |
| 430.00 | 6356.31 | 311.9 |
| 430.00 | 6606.63 | 323.008 |
| 430.00 | 7106.84 | 343.373 |
| 430.00 | 7106.87 | 343.374 |
| 430.00 | 7607.19 | 361.852 |
| 430.00 | 8107.49 | 378.831 |
| 430.00 | 8607.80 | 394.6 |
| 430.00 | 9108.14 | 409.364 |
| 430.00 | 9608.49 | 423.279 |
| 430.00 | 10108.80 | 436.468 |
| 430.00 | 11109.60 | 461.005 |
| 430.00 | 12110.40 | 483.546 |
| 430.00 | 13111.40 | 504.468 |
| 430.00 | 14111.80 | 524.058 |
| 430.00 | 15112.60 | 542.492 |
| 430.00 | 17614.00 | 584.593 |
| 430.00 | 20115.70 | 622.274 |
| 430.00 | 15112.60 | 542.492 |
| 430.00 | 17614.00 | 584.593 |
| 430.00 | 20115.70 | 622.274 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [195.15; 292.14] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41240e+01 | |||
| Coefficient B | -2.35413e+03 | |||
| Coefficient C | -2.50050e+01 | |||
| Temperature range, min. | 195.15 | |||
| Temperature range, max. | 292.14 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 200 250 | ||||
| Pvap | 1.33 | kPa | 195.15 | Calculated Property |
| Pvap | 3.04 | kPa | 205.93 | Calculated Property |
| Pvap | 6.32 | kPa | 216.70 | Calculated Property |
| Pvap | 12.15 | kPa | 227.48 | Calculated Property |
| Pvap | 21.86 | kPa | 238.26 | Calculated Property |
| Pvap | 37.18 | kPa | 249.03 | Calculated Property |
| Pvap | 60.23 | kPa | 259.81 | Calculated Property |
| Pvap | 93.51 | kPa | 270.59 | Calculated Property |
| Pvap | 139.92 | kPa | 281.36 | Calculated Property |
| Pvap | 202.65 | kPa | 292.14 | Calculated Property |
| Pvap | [6.69e-04; 3779.05] | kPa | [134.86; 425.18] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.87029e+01 | |||
| Coefficient B | -4.34663e+03 | |||
| Coefficient C | -6.92229e+00 | |||
| Coefficient D | 9.15271e-06 | |||
| Temperature range, min. | 134.86 | |||
| Temperature range, max. | 425.18 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 | ||||
| Pvap | 6.69e-04 | kPa | 134.86 | Calculated Property |
| Pvap | 0.08 | kPa | 167.12 | Calculated Property |
| Pvap | 1.84 | kPa | 199.38 | Calculated Property |
| Pvap | 15.42 | kPa | 231.63 | Calculated Property |
| Pvap | 71.77 | kPa | 263.89 | Calculated Property |
| Pvap | 229.21 | kPa | 296.15 | Calculated Property |
| Pvap | 569.65 | kPa | 328.41 | Calculated Property |
| Pvap | 1192.33 | kPa | 360.66 | Calculated Property |
| Pvap | 2214.06 | kPa | 392.92 | Calculated Property |
| Pvap | 3779.05 | kPa | 425.18 | Calculated Property |
Similar Compounds
Find more compounds similar to Butane.
Mixtures
- Squalane + Butane
- Butane + Ethyl Acetate
- Butane + Methyl Alcohol
- Isopropyl Alcohol + Butane
- Butane + 1-Butanol
- 2-Propanol, 2-methyl- + Butane
- Butane + Ethane, 1,1-difluoro-
- Dimethyl sulfide + Butane
- Butane + Diethyl sulfide
- Butane + Propanenitrile
- Butane + Ethanol
- Butane + Propene, hexafluoro-
- Butane + Hydrogen sulfide
- Propane + Butane
- Butane + Fluoroform
- Butane + Propane, 1,1,1,3,3-pentafluoro
- Ethane, hexafluoro- + Butane
- Butane + Dimethyl ether
- Difluoromethane + Butane
- Ethane, pentafluoro- + Butane
Find more mixtures with Butane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Measurements of the Liquid Viscosities of Mixtures of n-Butane, n-Hexane, and n-Octane with Squalane to 30MPa
- Thermophysical Properties of the Refrigerant Mixtures R417A and R417B from Dynamic Light Scattering (DLS)
- Measurement of the (p, rho, T) Properties for Pure Hydrocarbons at Temperatures up to 600 K and Pressures up to 200 MPa
- Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane
- Vapour-liquid equilibrium measurements and correlation for the pentafluoroethane (R125) + n-butane (R600) system
- Viscosity, density, interfacial tension and compositional data for near critical mixtures of methane + butane and methane + decane systems at 310.95K
- Henry s law constants of propane, propene, butane, and 2-methylpropane in methanol at 374-490K
- Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
- Vapor liquid equilibria for the binary system of 1,1-difluoroethane (HFC-152a) + n-butane (R-600) at various temperatures
- Isothermal binary vapour liquid equilibrium for butanes and butenes with dimethylsulphide
- Vapor liquid equilibrium in the n-butane +methanol system, measurement and modeling from 323.2 to 443.2K
- Vapor liquid equilibrium measurements and modeling of the n-butane + ethanol system from 323 to 423K
- Vapour liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
- Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
- High pressure vapor-liquid equilibria measurements and modeling of butane/ethanol system and isobutane/ethanol system
- Effects of association with impurities in ammonia purification
- Phase equilibrium data for mixtures involving 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane between 312 and 343 K
- An improved static-analytic apparatus for vapor-liquid equilibrium (PTxy) measurement using modified in-situ samplers
- Capillary constant and surface tension of dimethyl ether and n-butane at temperatures from 214 K to those close to the critical point
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
- Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
- Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
- Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
- Vapour pressure and excess Gibbs free energy of binary mixtures of hydrogen sulphide with ethane, propane, and n-butane at temperature of 182.33 K
- (pressure,density, temperature) Properties for n-butane in the temperature range from 280 K to 380 K at pressures up to 200 MPa
- Measurements of vapour pressures and saturated-liquid densities for n-butane at T = (280 to 424) K
- (Vapour + liquid) equilibria of the {1,1-difluoroethane (HFC-152a) + n-butane (HC-600)} system
- The (p,q,T,x) properties of (x1 propane + x2 n-butane) with x1 = (0.0000, 0.2729, 0.5021, and 0.7308) over the temperature range from (280 to 440) K at pressures from (1 to 200) MPa
- The (p, rho, T, x) properties for (x1 n-butane + x2 isobutane) with x1 = (0.2625, 0.4913, and 0.7508) in the temperature range from (280 to 440) K at pressures from (1 to 200) MPa
- The (p, rho, T, x) properties for (propane + n-butane + isobutane) ternary mixtures over the temperature range from (280 to 440) K at pressures from (1 to 200) MPa
- (Vapour + liquid) equilibria of the {trifluoromethane (HFC-23) + propane} and {trifluoromethane (HFC-23) + n-butane} systems
- (p, rho, T, x) properties for CO2/n-butane binary mixtures at T = (280 to 440) K and (3 to 200) MPa
- (Vapour + liquid + liquid) equilibrium measurements and correlation for the {1,1,1,2-tetrafluoroethane (R134a) + n-butane (R600)} system
- Isothermal (vapour + liquid) equilibrium measurements and correlation for the {n-butane (R600) + 1,1,1,3,3-pentafluoropropane (R245fa)} system at temperatures from (303.150 to 373.150) K
- Bubble Point Measurements of n-Butane + n-Octane and n-Butane + n-Nonane Binary Mixtures
- Reference Quality Vapor-Liquid Equilibrium Data for the Binary Systems Methane + Ethane, + Propane, + Butane and, + 2-Methylpropane, at Temperatures from (203 to 273) K and Pressures to 9 MPa
- Viscosity and dew point measurements of {xCH4 + (1- x)C4H10} for x = 0.9484 with a vibrating-wire viscometer.
- Viscosity and Density of Normal Butane Simultaneously Measured at Temperatures from (298 to 448) K and at Pressures up to 30 MPa Incorporating the Near-Critical Region
- Measurements of the Speed of Sound in Liquid n-Butane
- Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoroethane (R116) + n-Butane System at Temperatures from 273 to 323 K
- Density and Compressibility of Multicomponent n-Alkane Mixtures up to 463 K and 140 MPa
- Vapor-Liquid Equilibrium Measurements for 2,3,3,3-Tetrafluoroprop-1-ene + Butane at Temperatures from 283.15 to 323.15 K
- Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene, and 1,3-butadiene in 2-propanol at 250-330 K
- Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene and 1,3-Butadiene in 1-Butanol and 2-Butanol at (250 to 330) K
- Measurements of the Speed of Sound for Mixtures of Methane + Butane with a Particular Focus on the Critical State
- Critical Properties of Three Dimethyl Ether Binary Systems: Dimethyl Ether (RE-170) + Propane (HC-290), Butane (HC-600), and 2-Methyl Propane (HC-600A)
- Vapor-Liquid Equilibrium (VLE) Properties for the Binary Systems Propane (1) + n-Butane (2) and Propane (1) + Isobutane (3)
- Liquid-Phase Thermodynamic Properties for the Binary and Ternary Systems of Propane (1), n-Butane (2), and Isobutane (3)
- Liquid-Phase Thermodynamic Properties for Propane (1), n-Butane (2), and Isobutane (3)
- Henry's law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
- Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
- Vapor-Liquid Equilibrium for the Difluoromethane (R32) + n-Butane (R600) System
- Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
- 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
- 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
- Solubilities of Gases in the Ionic Liquid 1-n-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide
- Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
- Vapor-Liquid Equilibria of the 1,1,1-Trifluoroethane + n-Butane System
- 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
- Phase Behavior of the Butane + Decane Binary System
- Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
- Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
- Phase Equilibria of H2S-Hydrocarbons (Propane, n-Butane, and n-Pentane) Binary Systems at Low Temperatures
- Experimental Study of p-.rho.-T Relationship of Compressed Liquid Phase for Octafluoropropane and Two near Azeotropic Ternary HFC/HC Mixtures
- Validation of a New Apparatus Using the Dynamic Method for Determining the Critical Properties of Binary Gas/Gas Mixtures
- Bubble-Point Measurements of Eight Binary Mixtures for Organic Rankine Cycle Applications
- Isobaric Heat Capacity Measurements of Liquid Methane + Propane, Methane + Butane, and a Mixed Refrigerant by Differential Scanning Calorimetry at High Pressures and Low Temperatures
- New Vapor Liquid Liquid Equilibrium Solubility Data for iso-Butane, n-Butane, n-Pentane, and n-Hexane in Alkanolamine Aqueous Solutions
- Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
- 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
- Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
- Vapor-Liquid Equilibria for 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) + Butane (R600) at Various Temperatures
- Vapor-Liquid Equilibria for the Binary System of 1,1,1-Trifluoroethane (HFC-143a) + Butane (R600) at Various Temperatures
- Vapor-Liquid Equilibria for Propane (R290) + n-Butane (R600) at Various Temperatures
- Vapor-Liquid Equilibrium for 1-Butanol + 1-Butene at (318.4 and 364.5) K and Vapor-Liquid Equilibrium of 1-Butanol + 2-Methylpropane, + n-Butane and 1-Butene + 2-Methylpropane at 318.4 K
- In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
- Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
- Isothermal Binary Vapor-Liquid Equilibrium for 2-Methylpropane and n-Butane with 1,2-Ethanedithiol and 2-Methyl-2-propanethiol
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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