Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2180 | KDB | |
ΔcH°liquid | [-474.00; -473.21] | kJ/mol |
![]() |
ΔcH°liquid | -473.21 | kJ/mol | NIST |
ΔcH°liquid | -474.00 ± 8.40 | kJ/mol | NIST |
μ | 1.10 | debye | KDB |
EA | [0.62; 1.76] | eV |
![]() |
EA | 0.62 ± 0.16 | eV | NIST |
EA | 1.76 ± 0.05 | eV | NIST |
ΔfG° | -68.58 | kJ/mol | KDB |
Rg | 3.1780 | KDB | |
ΔfH°gas | [-102.90; -101.30] | kJ/mol |
![]() |
ΔfH°gas | -101.30 | kJ/mol | KDB |
ΔfH°gas | -102.90 ± 2.50 | kJ/mol | NIST |
ΔfH°liquid | [-134.30; -134.10] | kJ/mol |
![]() |
ΔfH°liquid | -134.10 ± 2.50 | kJ/mol | NIST |
ΔfH°liquid | -134.30 | kJ/mol | NIST |
ΔfusH° | 7.41 | kJ/mol | Joback Calculated Property |
ΔvapH° | [30.50; 31.40] | kJ/mol |
![]() |
ΔvapH° | 31.40 | kJ/mol | NIST |
ΔvapH° | 31.32 ± 0.08 | kJ/mol | NIST |
ΔvapH° | 31.10 | kJ/mol | NIST |
ΔvapH° | 30.50 ± 0.42 | kJ/mol | NIST |
IE | [11.30; 11.50] | eV |
![]() |
IE | 11.37 ± 0.02 | eV | NIST |
IE | 11.41 ± 0.02 | eV | NIST |
IE | 11.30 | eV | NIST |
IE | 11.48 | eV | NIST |
IE | 11.37 ± 0.02 | eV | NIST |
IE | 11.40 | eV | NIST |
IE | 11.50 | eV | NIST |
IE | 11.42 ± 0.03 | eV | NIST |
IE | 11.50 | eV | NIST |
IE | 11.48 | eV | NIST |
log10WS | [-1.17; -1.17] |
![]() |
|
log10WS | -1.17 | Estimat... | |
log10WS | -1.17 | Aq. Sol... | |
logPoct/wat | 1.986 | Crippen Calculated Property | |
McVol | 61.670 | ml/mol | McGowan Calculated Property |
NFPA Health | 2 | KDB | |
Pc | [5328.68; 5470.00] | kPa |
![]() |
Pc | 5470.00 | kPa | KDB |
Pc | 5328.68 ± 10.13 | kPa | NIST |
Pc | 5328.68 ± 6.07 | kPa | NIST |
ρc | [458.41; 495.42] | kg/m3 |
![]() |
ρc | 490.64 ± 3.58 | kg/m3 | NIST |
ρc | 458.41 ± 2.39 | kg/m3 | NIST |
ρc | 495.42 ± 2.39 | kg/m3 | NIST |
Inp | [561.00; 630.00] |
![]() |
|
Inp | 617.20 | NIST | |
Inp | 619.00 | NIST | |
Inp | 628.40 | NIST | |
Inp | 625.80 | NIST | |
Inp | 621.10 | NIST | |
Inp | 618.20 | NIST | |
Inp | 614.80 | NIST | |
Inp | 607.90 | NIST | |
Inp | 604.00 | NIST | |
Inp | 606.00 | NIST | |
Inp | 604.00 | NIST | |
Inp | 606.80 | NIST | |
Inp | 610.00 | NIST | |
Inp | 604.00 | NIST | |
Inp | 608.00 | NIST | |
Inp | 602.00 | NIST | |
Inp | 582.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | Outlier 568.00 | NIST | |
Inp | 595.20 | NIST | |
Inp | 616.00 | NIST | |
Inp | 610.00 | NIST | |
Inp | 587.00 | NIST | |
Inp | 622.00 | NIST | |
Inp | 622.00 | NIST | |
Inp | 613.00 | NIST | |
Inp | 598.00 | NIST | |
Inp | 601.00 | NIST | |
Inp | 616.00 | NIST | |
Inp | 615.00 | NIST | |
Inp | 601.00 | NIST | |
Inp | 621.70 | NIST | |
Inp | 601.00 | NIST | |
Inp | 590.00 | NIST | |
Inp | 618.00 | NIST | |
Inp | 600.00 | NIST | |
Inp | Outlier 561.00 | NIST | |
Inp | Outlier 569.00 | NIST | |
Inp | 630.00 | NIST | |
Inp | 605.00 | NIST | |
Inp | 615.00 | NIST | |
Inp | 601.00 | NIST | |
Inp | 615.00 | NIST | |
Inp | 618.00 | NIST | |
Inp | 618.00 | NIST | |
Inp | 600.00 | NIST | |
Inp | 588.00 | NIST | |
Inp | 601.00 | NIST | |
Inp | 616.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 617.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 611.00 | NIST | |
Inp | 629.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 603.00 | NIST | |
Inp | 620.00 | NIST | |
Inp | 618.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 601.00 | NIST | |
Inp | 601.00 | NIST | |
Inp | 603.00 | NIST | |
Inp | 605.00 | NIST | |
Inp | 620.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 611.00 | NIST | |
Inp | 601.00 | NIST | |
Inp | 606.00 | NIST | |
Inp | 603.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 616.00 | NIST | |
Inp | 595.00 | NIST | |
Inp | 605.00 | NIST | |
Inp | 605.00 | NIST | |
Inp | 598.00 | NIST | |
I | [992.00; 1045.00] |
![]() |
|
I | 1037.00 | NIST | |
I | 1037.00 | NIST | |
I | 1034.00 | NIST | |
I | 1030.11 | NIST | |
I | 1028.95 | NIST | |
I | 1027.69 | NIST | |
I | 1026.00 | NIST | |
I | 1026.00 | NIST | |
I | 1024.00 | NIST | |
I | 1021.00 | NIST | |
I | 1020.00 | NIST | |
I | 1022.00 | NIST | |
I | 1026.00 | NIST | |
I | 1026.00 | NIST | |
I | 1013.00 | NIST | |
I | 1028.00 | NIST | |
I | 1010.00 | NIST | |
I | 1020.00 | NIST | |
I | 1021.00 | NIST | |
I | 1022.00 | NIST | |
I | 1022.00 | NIST | |
I | 1018.00 | NIST | |
I | 1020.00 | NIST | |
I | 1023.00 | NIST | |
I | 1022.00 | NIST | |
I | Outlier 999.00 | NIST | |
I | 1038.00 | NIST | |
I | 1010.00 | NIST | |
I | Outlier 1045.00 | NIST | |
I | 1007.00 | NIST | |
I | 1037.00 | NIST | |
I | 1037.00 | NIST | |
I | 1017.00 | NIST | |
I | 1025.00 | NIST | |
I | 1015.00 | NIST | |
I | 1016.00 | NIST | |
I | 1037.00 | NIST | |
I | 1037.00 | NIST | |
I | 1018.00 | NIST | |
I | 1020.00 | NIST | |
I | Outlier 992.00 | NIST | |
I | 1014.00 | NIST | |
I | 1014.00 | NIST | |
I | 1000.00 | NIST | |
I | 1000.00 | NIST | |
I | 1024.00 | NIST | |
I | 1037.00 | NIST | |
I | 1027.69 | NIST | |
I | 1010.00 | NIST | |
I | 1024.00 | NIST | |
Tboil | [333.95; 335.00] | K |
![]() |
Tboil | 334.32 | K | KDB |
Tboil | Outlier 335.00 | K | The rol... |
Tboil | 334.10 | K | Phase d... |
Tboil | 334.35 | K | Separat... |
Tboil | 334.12 | K | Isobari... |
Tboil | 334.30 | K | NIST |
Tboil | 334.37 ± 0.15 | K | NIST |
Tboil | 334.45 ± 0.50 | K | NIST |
Tboil | 334.10 ± 0.30 | K | NIST |
Tboil | 334.35 ± 0.06 | K | NIST |
Tboil | 334.34 ± 0.25 | K | NIST |
Tboil | 334.39 ± 0.30 | K | NIST |
Tboil | 334.30 ± 0.20 | K | NIST |
Tboil | 334.35 ± 0.10 | K | NIST |
Tboil | 334.24 ± 0.15 | K | NIST |
Tboil | Outlier 333.95 ± 0.40 | K | NIST |
Tboil | 334.42 ± 0.35 | K | NIST |
Tboil | 334.42 ± 0.30 | K | NIST |
Tboil | 334.35 ± 0.30 | K | NIST |
Tboil | 334.35 ± 0.30 | K | NIST |
Tboil | 334.35 ± 0.30 | K | NIST |
Tboil | 334.30 ± 0.20 | K | NIST |
Tboil | 334.30 ± 0.50 | K | NIST |
Tboil | 334.45 ± 0.50 | K | NIST |
Tboil | 334.20 ± 1.00 | K | NIST |
Tboil | 334.50 ± 0.20 | K | NIST |
Tboil | 334.22 ± 0.50 | K | NIST |
Tboil | 334.27 ± 0.30 | K | NIST |
Tboil | 334.30 ± 0.25 | K | NIST |
Tboil | 334.30 ± 0.50 | K | NIST |
Tboil | 334.23 ± 0.06 | K | NIST |
Tboil | 334.30 ± 0.30 | K | NIST |
Tboil | 334.40 ± 0.50 | K | NIST |
Tboil | 334.37 ± 0.20 | K | NIST |
Tboil | 334.20 ± 0.30 | K | NIST |
Tboil | 334.22 ± 0.20 | K | NIST |
Tboil | 334.35 ± 0.30 | K | NIST |
Tboil | 334.30 ± 0.50 | K | NIST |
Tboil | 334.15 ± 0.50 | K | NIST |
Tboil | 334.40 ± 0.30 | K | NIST |
Tboil | 334.35 ± 0.20 | K | NIST |
Tboil | 334.45 ± 0.60 | K | NIST |
Tc | 536.40 | K | KDB |
Tfus | [209.50; 212.15] | K |
![]() |
Tfus | 209.50 | K | KDB |
Tfus | 209.95 | K | Aq. Sol... |
Tfus | 209.73 ± 0.01 | K | NIST |
Tfus | 209.64 ± 0.10 | K | NIST |
Tfus | 210.15 ± 1.00 | K | NIST |
Tfus | 209.61 ± 0.08 | K | NIST |
Tfus | 209.65 ± 0.20 | K | NIST |
Tfus | 211.05 ± 0.30 | K | NIST |
Tfus | 209.50 ± 0.70 | K | NIST |
Tfus | 210.00 ± 2.00 | K | NIST |
Tfus | 209.65 ± 0.20 | K | NIST |
Tfus | 211.59 ± 0.50 | K | NIST |
Tfus | 209.90 ± 0.30 | K | NIST |
Tfus | Outlier 212.15 ± 1.00 | K | NIST |
Tfus | 210.46 ± 0.20 | K | NIST |
Tfus | 210.00 ± 2.00 | K | NIST |
Ttriple | 209.61 ± 0.20 | K | NIST |
Vc | 0.239 | m3/kmol | KDB |
Vm | 8.07e-05 | m3/mol | Excess ... |
Zc | 0.2931300 | KDB | |
Zra | 0.28 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [71.18; 82.74] | J/mol×K | [334.13; 532.11] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 72 74 76 78 80 82 350 400 450 500 | ||||
Cp,gas | 71.18 | J/mol×K | 334.13 | Joback Calculated Property |
Cp,gas | 73.44 | J/mol×K | 367.13 | Joback Calculated Property |
Cp,gas | 75.56 | J/mol×K | 400.12 | Joback Calculated Property |
Cp,gas | 77.54 | J/mol×K | 433.12 | Joback Calculated Property |
Cp,gas | 79.40 | J/mol×K | 466.12 | Joback Calculated Property |
Cp,gas | 81.13 | J/mol×K | 499.12 | Joback Calculated Property |
Cp,gas | 82.74 | J/mol×K | 532.11 | Joback Calculated Property |
Cp,liquid | [113.00; 139.70] | J/mol×K | [293.00; 303.60] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 115 120 125 130 135 140 295 300 | ||||
Cp,liquid | 116.20 | J/mol×K | 293.00 | NIST |
Cp,liquid | 115.50 | J/mol×K | 293.20 | NIST |
Cp,liquid | 117.10 | J/mol×K | 298.00 | NIST |
Cp,liquid | 114.18 | J/mol×K | 298.00 | NIST |
Cp,liquid | 113.00 | J/mol×K | 298.10 | NIST |
Cp,liquid | 114.25 | J/mol×K | 298.15 | NIST |
Cp,liquid | 115.50 | J/mol×K | 298.15 | NIST |
Cp,liquid | 113.73 | J/mol×K | 298.15 | NIST |
Cp,liquid | 114.26 | J/mol×K | 298.15 | NIST |
Cp,liquid | 113.85 | J/mol×K | 298.15 | NIST |
Cp,liquid | 115.50 | J/mol×K | 298.15 | NIST |
Cp,liquid | 114.35 | J/mol×K | 298.15 | NIST |
Cp,liquid | 114.32 | J/mol×K | 298.15 | NIST |
Cp,liquid | 113.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 113.40 | J/mol×K | 300.00 | NIST |
Cp,liquid | 116.70 | J/mol×K | 303.00 | NIST |
Cp,liquid | 114.00 | J/mol×K | 303.20 | NIST |
Cp,liquid | 139.70 | J/mol×K | 303.60 | NIST |
η | [0.0004710; 0.0007130] | Pa×s | [273.15; 318.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 4.50e-4 5.00e-4 5.50e-4 6.00e-4 6.50e-4 7.00e-4 280 290 300 310 | ||||
η | 0.0007130 | Pa×s | 273.15 | Density... |
η | 0.0006510 | Pa×s | 283.15 | Density... |
η | 0.0006000 | Pa×s | 293.15 | Density... |
η | 0.0005560 | Pa×s | 298.15 | Densiti... |
η | 0.0005760 | Pa×s | 298.15 | Density... |
η | 0.0005340 | Pa×s | 303.15 | Densiti... |
η | 0.0005340 | Pa×s | 303.15 | Densiti... |
η | 0.0005200 | Pa×s | 303.15 | Studies... |
η | 0.0005520 | Pa×s | 303.15 | Density... |
η | 0.0005130 | Pa×s | 308.15 | Densiti... |
η | 0.0004910 | Pa×s | 313.15 | Densiti... |
η | 0.0004910 | Pa×s | 313.15 | Densiti... |
η | 0.0004710 | Pa×s | 313.15 | Studies... |
η | 0.0005090 | Pa×s | 313.15 | Density... |
η | 0.0004910 | Pa×s | 318.15 | Density... |
ΔfusH | [8.80; 8.80] | kJ/mol | [209.60; 209.60] | ![]() |
ΔfusH | 8.80 | kJ/mol | 209.60 | NIST |
ΔfusH | 8.80 | kJ/mol | 209.60 | NIST |
ΔvapH | [28.90; 35.00] | kJ/mol | [248.00; 501.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 29 30 31 32 33 34 35 300 400 500 | ||||
ΔvapH | 31.80 | kJ/mol | 248.00 | NIST |
ΔvapH | 35.00 | kJ/mol | 274.50 | NIST |
ΔvapH | 32.50 | kJ/mol | 296.50 | NIST |
ΔvapH | 30.90 | kJ/mol | 320.50 | NIST |
ΔvapH | 29.71 | kJ/mol | 334.30 | KDB |
ΔvapH | 29.24 | kJ/mol | 334.30 | NIST |
ΔvapH | 30.80 | kJ/mol | 366.50 | NIST |
ΔvapH | 30.40 | kJ/mol | 374.50 | NIST |
ΔvapH | 28.90 | kJ/mol | 445.50 | NIST |
ΔvapH | 30.10 | kJ/mol | 501.00 | NIST |
ν | [0.0000003; 0.0000004] | m2/s | [303.15; 313.15] | ![]() |
ν | 0.0000004 | m2/s | 303.15 | Densiti... |
ν | 0.0000003 | m2/s | 313.15 | Densiti... |
Pvap | [32.19; 129.28] | kPa | [303.15; 342.00] | ![]() |
T(K) Vapor pressure (kPa) 40 60 80 100 120 310 320 330 340 | ||||
Pvap | 32.19 | kPa | 303.15 | Density... |
Pvap | 32.41 | kPa | 303.15 | Total V... |
Pvap | 32.19 | kPa | 303.15 | Density... |
Pvap | 34.81 | kPa | 305.00 | Isobari... |
Pvap | 42.47 | kPa | 310.00 | Isobari... |
Pvap | 51.43 | kPa | 315.00 | Isobari... |
Pvap | 61.85 | kPa | 320.00 | Isobari... |
Pvap | 73.88 | kPa | 325.00 | Isobari... |
Pvap | 87.71 | kPa | 330.00 | Isobari... |
Pvap | 101.30 | kPa | 334.12 | Isobari... |
Pvap | 101.30 | kPa | 334.35 | Separat... |
Pvap | 103.50 | kPa | 335.00 | Isobari... |
Pvap | 121.45 | kPa | 340.00 | Isobari... |
Pvap | 129.28 | kPa | 342.00 | Isobari... |
n0 | [1.44100; 1.45000] | [283.15; 303.15] | ![]() |
|
T(K) Refractive Index 1.44 1.44 1.45 1.45 1.45 285 290 295 300 | ||||
n0 | 1.45000 | 283.15 | Partial... | |
n0 | 1.44710 | 288.15 | Partial... | |
n0 | 1.44760 | 293.15 | Solubil... | |
n0 | 1.44390 | 293.15 | Partial... | |
n0 | 1.44280 | 298.15 | Vapour ... | |
n0 | 1.44300 | 298.15 | Liquid-... | |
n0 | 1.44200 | 298.15 | Partial... | |
n0 | 1.44290 | 298.15 | Study o... | |
n0 | 1.44100 | 303.15 | Densiti... | |
ρl | [1429.89; 1498.14] | kg/m3 | [288.15; 323.15] | ![]() |
T(K) Liquid Density (kg/m3) 1430 1440 1450 1460 1470 1480 1490 1500 290 300 310 320 | ||||
ρl | 1498.08 | kg/m3 | 288.15 | Volumet... |
ρl | 1498.08 | kg/m3 | 288.15 | Tempera... |
ρl | 1491.86 | kg/m3 | 288.15 | Densiti... |
ρl | 1498.08 | kg/m3 | 288.15 | Densiti... |
ρl | 1498.08 | kg/m3 | 288.15 | Volumet... |
ρl | 1498.14 | kg/m3 | 288.15 | Volumet... |
ρl | 1492.31 | kg/m3 | 288.15 | Densiti... |
ρl | 1489.00 | kg/m3 | 293.00 | KDB |
ρl | 1488.70 | kg/m3 | 293.15 | Excess ... |
ρl | 1488.64 | kg/m3 | 293.15 | Volumet... |
ρl | 1488.64 | kg/m3 | 293.15 | Densiti... |
ρl | 1488.64 | kg/m3 | 293.15 | Volumet... |
ρl | 1488.70 | kg/m3 | 293.15 | Volumet... |
ρl | 1488.64 | kg/m3 | 293.15 | Tempera... |
ρl | 1487.63 | kg/m3 | 293.15 | Speed o... |
ρl | 1483.02 | kg/m3 | 293.20 | Isobari... |
ρl | 1478.16 | kg/m3 | 298.15 | Speed o... |
ρl | 1478.75 | kg/m3 | 298.15 | Densiti... |
ρl | 1473.42 | kg/m3 | 298.15 | Volumet... |
ρl | 1479.15 | kg/m3 | 298.15 | Volumet... |
ρl | 1473.43 | kg/m3 | 298.15 | Densiti... |
ρl | 1479.15 | kg/m3 | 298.15 | Tempera... |
ρl | 1479.21 | kg/m3 | 298.15 | Volumet... |
ρl | 1473.16 | kg/m3 | 298.15 | Densiti... |
ρl | 1479.15 | kg/m3 | 298.15 | Densiti... |
ρl | 1479.15 | kg/m3 | 298.15 | Volumet... |
ρl | 1480.34 | kg/m3 | 298.20 | The cho... |
ρl | 1475.30 | kg/m3 | 303.00 | Thermo-... |
ρl | 1475.30 | kg/m3 | 303.00 | Thermo-... |
ρl | 1468.61 | kg/m3 | 303.15 | Speed o... |
ρl | 1469.63 | kg/m3 | 303.15 | Volumet... |
ρl | 1469.61 | kg/m3 | 303.15 | Densiti... |
ρl | 1469.61 | kg/m3 | 303.15 | Volumet... |
ρl | 1469.61 | kg/m3 | 303.15 | Volumet... |
ρl | 1470.50 | kg/m3 | 303.15 | Viscosi... |
ρl | 1469.61 | kg/m3 | 303.15 | Tempera... |
ρl | 1469.16 | kg/m3 | 303.15 | Densiti... |
ρl | 1469.69 | kg/m3 | 303.15 | Excess ... |
ρl | 1470.80 | kg/m3 | 308.00 | Thermo-... |
ρl | 1470.80 | kg/m3 | 308.00 | Thermo-... |
ρl | 1459.00 | kg/m3 | 308.15 | Speed o... |
ρl | 1460.01 | kg/m3 | 308.15 | Densiti... |
ρl | 1454.33 | kg/m3 | 308.15 | Volumet... |
ρl | 1454.33 | kg/m3 | 308.15 | Densiti... |
ρl | 1460.03 | kg/m3 | 308.15 | Tempera... |
ρl | 1460.03 | kg/m3 | 308.15 | Volumet... |
ρl | 1460.03 | kg/m3 | 308.15 | Densiti... |
ρl | 1454.07 | kg/m3 | 308.15 | Densiti... |
ρl | 1460.03 | kg/m3 | 308.15 | Volumet... |
ρl | 1465.80 | kg/m3 | 313.00 | Thermo-... |
ρl | 1465.80 | kg/m3 | 313.00 | Thermo-... |
ρl | 1450.39 | kg/m3 | 313.15 | Excess ... |
ρl | 1450.41 | kg/m3 | 313.15 | Volumet... |
ρl | 1450.41 | kg/m3 | 313.15 | Densiti... |
ρl | 1450.41 | kg/m3 | 313.15 | Volumet... |
ρl | 1450.41 | kg/m3 | 313.15 | Tempera... |
ρl | 1450.39 | kg/m3 | 313.15 | Densiti... |
ρl | 1434.72 | kg/m3 | 318.15 | Densiti... |
ρl | 1440.03 | kg/m3 | 318.15 | Densiti... |
ρl | 1434.97 | kg/m3 | 318.15 | Densiti... |
ρl | 1434.98 | kg/m3 | 318.15 | Volumet... |
ρl | 1429.89 | kg/m3 | 323.15 | Excess ... |
csound,fluid | [916.63; 984.42] | m/s | [298.15; 318.15] | ![]() |
csound,fluid | 984.42 | m/s | 298.15 | Speeds ... |
csound,fluid | 950.45 | m/s | 308.15 | Speeds ... |
csound,fluid | 916.63 | m/s | 318.15 | Speeds ... |
γ | [0.03; 0.03] | N/m | [293.15; 298.20] | ![]() |
γ | 0.03 | N/m | 293.15 | Investi... |
γ | 0.03 | N/m | 298.20 | KDB |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboil | 334.25 | K | 96.60 | Low cos... |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
303.15 | 101.30 | 0.0005 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
303.15 | 101.30 | 0.0005 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 5482.48] | kPa | [244.65; 536.40] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43630e+01 | |||
Coefficient B | -2.83926e+03 | |||
Coefficient C | -4.29370e+01 | |||
Temperature range, min. | 244.65 | |||
Temperature range, max. | 536.40 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 | ||||
Pvap | 1.33 | kPa | 244.65 | Calculated Property |
Pvap | 9.36 | kPa | 277.07 | Calculated Property |
Pvap | 40.90 | kPa | 309.48 | Calculated Property |
Pvap | 129.81 | kPa | 341.90 | Calculated Property |
Pvap | 328.67 | kPa | 374.32 | Calculated Property |
Pvap | 705.23 | kPa | 406.73 | Calculated Property |
Pvap | 1335.51 | kPa | 439.15 | Calculated Property |
Pvap | 2296.22 | kPa | 471.57 | Calculated Property |
Pvap | 3658.33 | kPa | 503.98 | Calculated Property |
Pvap | 5482.48 | kPa | 536.40 | Calculated Property |
Pvap | [0.08; 5628.11] | kPa | [209.63; 536.40] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.11439e+01 | |||
Coefficient B | -6.35114e+03 | |||
Coefficient C | -1.00709e+01 | |||
Coefficient D | 9.12761e-06 | |||
Temperature range, min. | 209.63 | |||
Temperature range, max. | 536.40 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 | ||||
Pvap | 0.08 | kPa | 209.63 | Calculated Property |
Pvap | 1.54 | kPa | 245.94 | Calculated Property |
Pvap | 12.69 | kPa | 282.25 | Calculated Property |
Pvap | 59.51 | kPa | 318.55 | Calculated Property |
Pvap | 192.92 | kPa | 354.86 | Calculated Property |
Pvap | 487.71 | kPa | 391.17 | Calculated Property |
Pvap | 1039.15 | kPa | 427.48 | Calculated Property |
Pvap | 1965.80 | kPa | 463.78 | Calculated Property |
Pvap | 3422.90 | kPa | 500.09 | Calculated Property |
Pvap | 5628.11 | kPa | 536.40 | Calculated Property |
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