Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2510 | KDB | |
ΔcH°gas | -1008.00 ± 2.00 | kJ/mol | NIST |
μ | 2.30 | debye | KDB |
ΔfG° | -679.20 | kJ/mol | KDB |
ΔfH°gas | [-749.00; -746.10] | kJ/mol |
![]() |
ΔfH°gas | -746.10 | kJ/mol | KDB |
ΔfH°gas | -748.70 ± 3.20 | kJ/mol | NIST |
ΔfH°gas | -749.00 ± 2.00 | kJ/mol | NIST |
ΔfusH° | 2.76 | kJ/mol | Joback Calculated Property |
ΔvapH° | 16.30 | kJ/mol | Joback Calculated Property |
IE | [12.90; 13.80] | eV |
![]() |
IE | 13.30 ± 0.10 | eV | NIST |
IE | 13.80 | eV | NIST |
IE | 12.90 ± 0.10 | eV | NIST |
log10WS | -1.32 | Crippen Calculated Property | |
logPoct/wat | 1.569 | Crippen Calculated Property | |
McVol | 44.350 | ml/mol | McGowan Calculated Property |
Pc | [3411.60; 3769.00] | kPa |
![]() |
Pc | 3760.00 | kPa | KDB |
Pc | 3763.90 ± 5.00 | kPa | NIST |
Pc | 3411.60 ± 5.00 | kPa | NIST |
Pc | 3769.00 ± 5.00 | kPa | NIST |
Pc | 3757.63 ± 103.42 | kPa | NIST |
ρc | [428.61; 433.65] | kg/m3 |
![]() |
ρc | 433.65 ± 3.36 | kg/m3 | NIST |
ρc | 433.65 ± 1.68 | kg/m3 | NIST |
ρc | 428.61 ± 3.36 | kg/m3 | NIST |
ρc | 433.65 ± 15.13 | kg/m3 | NIST |
Inp | 268.00 | NIST | |
S°liquid | 224.10 | J/mol×K | NIST |
Tboil | [225.60; 226.45] | K |
![]() |
Tboil | 225.60 | K | KDB |
Tboil | 226.00 | K | NIST |
Tboil | 226.45 ± 0.10 | K | NIST |
Tc | [345.86; 346.30] | K |
![]() |
Tc | 346.30 | K | KDB |
Tc | 345.86 ± 0.05 | K | NIST |
Tc | 345.86 ± 0.02 | K | NIST |
Tc | 345.97 ± 0.20 | K | NIST |
Tc | 346.25 ± 0.70 | K | NIST |
Tfus | 161.80 | K | KDB |
Ttriple | 161.82 ± 0.02 | K | NIST |
Vc | 0.194 | m3/kmol | KDB |
Zc | 0.2533380 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [63.79; 90.91] | J/mol×K | [239.74; 378.57] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 65 70 75 80 85 90 250 300 350 | ||||
Cp,gas | 63.79 | J/mol×K | 239.74 | Joback Calculated Property |
Cp,gas | 68.89 | J/mol×K | 262.88 | Joback Calculated Property |
Cp,gas | 73.75 | J/mol×K | 286.02 | Joback Calculated Property |
Cp,gas | 78.37 | J/mol×K | 309.15 | Joback Calculated Property |
Cp,gas | 82.77 | J/mol×K | 332.29 | Joback Calculated Property |
Cp,gas | 86.95 | J/mol×K | 355.43 | Joback Calculated Property |
Cp,gas | 90.91 | J/mol×K | 378.57 | Joback Calculated Property |
Cp,liquid | [109.66; 224.39] | J/mol×K | [220.00; 350.00] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 100 120 140 160 180 200 220 250 300 350 | ||||
Cp,liquid | 109.66 | J/mol×K | 220.00 | NIST |
Cp,liquid | 136.15 | J/mol×K | 310.00 | Measure... |
Cp,liquid | 140.35 | J/mol×K | 315.00 | Measure... |
Cp,liquid | 145.39 | J/mol×K | 320.00 | Measure... |
Cp,liquid | 150.43 | J/mol×K | 325.00 | Measure... |
Cp,liquid | 155.47 | J/mol×K | 330.00 | Measure... |
Cp,liquid | 162.20 | J/mol×K | 335.00 | Measure... |
Cp,liquid | 173.96 | J/mol×K | 340.00 | Measure... |
Cp,liquid | 189.93 | J/mol×K | 345.00 | Measure... |
Cp,liquid | 192.45 | J/mol×K | 345.00 | Measure... |
Cp,liquid | 224.39 | J/mol×K | 350.00 | Measure... |
ΔfusH | [0.30; 6.19] | kJ/mol | [156.40; 161.90] | ![]() |
ΔfusH | 0.30 | kJ/mol | 156.40 | NIST |
ΔfusH | 6.19 | kJ/mol | 161.80 | NIST |
ΔfusH | 6.19 | kJ/mol | 161.90 | NIST |
ΔfusH | 6.19 | kJ/mol | 161.90 | NIST |
ΔvapH | [8.70; 20.50] | kJ/mol | [200.00; 333.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 8 10 12 14 16 18 20 200 250 300 | ||||
ΔvapH | 20.50 | kJ/mol | 200.00 | NIST |
ΔvapH | 19.20 ± 0.10 | kJ/mol | 224.00 | NIST |
ΔvapH | 19.18 | kJ/mol | 224.40 | NIST |
ΔvapH | 19.16 | kJ/mol | 225.70 | KDB |
ΔvapH | 18.90 | kJ/mol | 233.00 | NIST |
ΔvapH | 18.10 | kJ/mol | 258.00 | NIST |
ΔvapH | 17.50 | kJ/mol | 258.00 | NIST |
ΔvapH | 16.70 | kJ/mol | 258.00 | NIST |
ΔvapH | 15.90 | kJ/mol | 258.00 | NIST |
ΔvapH | 16.40 | kJ/mol | 273.00 | NIST |
ΔvapH | 13.80 | kJ/mol | 303.00 | NIST |
ΔvapH | 8.70 | kJ/mol | 333.00 | NIST |
Pvap | [529.20; 3553.00] | kPa | [268.15; 343.15] | ![]() |
T(K) Vapor pressure (kPa) 500 1000 1500 2000 2500 3000 3500 280 300 320 340 | ||||
Pvap | 529.20 | kPa | 268.15 | Measure... |
Pvap | 626.00 | kPa | 273.15 | (Vapour... |
Pvap | 620.00 | kPa | 273.15 | Vapor-L... |
Pvap | 722.40 | kPa | 278.15 | Measure... |
Pvap | 838.60 | kPa | 283.15 | Vapor-l... |
Pvap | 837.00 | kPa | 283.15 | Vapor-L... |
Pvap | 962.00 | kPa | 288.15 | Measure... |
Pvap | 972.00 | kPa | 288.15 | (Vapour... |
Pvap | 1104.00 | kPa | 293.15 | Vapor-L... |
Pvap | 1107.90 | kPa | 293.15 | Vapor-l... |
Pvap | 1261.80 | kPa | 298.15 | Measure... |
Pvap | 1432.00 | kPa | 303.15 | Vapor-L... |
Pvap | 1442.00 | kPa | 303.15 | (Vapour... |
Pvap | 1435.20 | kPa | 303.15 | Vapor-l... |
Pvap | 1619.80 | kPa | 308.15 | Measure... |
Pvap | 1831.00 | kPa | 313.15 | Vapor-L... |
Pvap | 1831.00 | kPa | 313.15 | Vapor l... |
Pvap | 1830.00 | kPa | 313.15 | Vapor-L... |
Pvap | 1831.00 | kPa | 313.15 | Vapor l... |
Pvap | 1834.00 | kPa | 313.15 | Vapor-l... |
Pvap | 2063.00 | kPa | 318.15 | (Vapour... |
Pvap | 2055.20 | kPa | 318.15 | Measure... |
Pvap | 2309.70 | kPa | 323.15 | Vapor-l... |
Pvap | 2307.00 | kPa | 323.15 | Vapor l... |
Pvap | 2302.00 | kPa | 323.15 | Vapor-L... |
Pvap | 2302.00 | kPa | 323.15 | Vapor l... |
Pvap | 2298.00 | kPa | 323.15 | Vapor-L... |
Pvap | 2874.00 | kPa | 333.15 | Vapor l... |
Pvap | 2874.00 | kPa | 333.15 | Vapor-L... |
Pvap | 2874.00 | kPa | 333.15 | Vapor l... |
Pvap | 2875.00 | kPa | 333.15 | (Vapour... |
Pvap | 3553.00 | kPa | 343.15 | Vapor l... |
Pvap | 3553.00 | kPa | 343.15 | Vapor-L... |
ΔfusS | [1.90; 38.30] | J/mol×K | [156.40; 161.90] | ![]() |
ΔfusS | 38.30 | J/mol×K | 156.40 | NIST |
ΔfusS | 1.90 | J/mol×K | 161.90 | NIST |
ΔvapS | 85.45 | J/mol×K | 224.40 | NIST |
Fixed | Measured | |
---|---|---|
Temperature, K - Gas | Pressure, kPa - Gas | Molar heat capacity at constant pressure, J/K/mol - Gas |
311.15 | 1600.00 | 120.18 |
317.15 | 1800.00 | 125.89 |
318.15 | 1600.00 | 111.77 |
318.15 | 2000.00 | 139.51 |
324.15 | 2200.00 | 145.31 |
326.15 | 2400.00 | 161.69 |
327.15 | 2400.00 | 160.77 |
338.15 | 2400.00 | 130.60 |
341.15 | 2200.00 | 117.24 |
343.15 | 2400.00 | 124.80 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
254.35 | 1340.00 | 0.0002 |
254.35 | 1350.00 | 0.0002 |
254.35 | 1360.00 | 0.0002 |
254.35 | 1410.00 | 0.0002 |
254.35 | 1450.00 | 0.0002 |
254.35 | 1960.00 | 0.0002 |
254.35 | 1970.00 | 0.0002 |
254.35 | 2010.00 | 0.0002 |
254.35 | 2040.00 | 0.0002 |
254.35 | 2070.00 | 0.0002 |
254.35 | 3110.00 | 0.0002 |
254.35 | 3160.00 | 0.0002 |
254.35 | 3170.00 | 0.0002 |
254.35 | 3210.00 | 0.0002 |
254.35 | 3280.00 | 0.0002 |
254.35 | 3320.00 | 0.0002 |
254.35 | 4170.00 | 0.0002 |
254.35 | 4190.00 | 0.0002 |
254.35 | 4210.00 | 0.0002 |
254.35 | 4940.00 | 0.0002 |
254.35 | 4970.00 | 0.0002 |
254.35 | 5000.00 | 0.0002 |
254.35 | 5020.00 | 0.0002 |
254.35 | 5050.00 | 0.0002 |
254.35 | 5100.00 | 0.0002 |
254.35 | 1350.00 | 0.0002 |
254.35 | 1360.00 | 0.0002 |
254.35 | 1960.00 | 0.0002 |
254.35 | 2010.00 | 0.0002 |
254.35 | 4210.00 | 0.0002 |
254.35 | 1350.00 | 0.0002 |
263.02 | 1300.00 | 0.0002 |
263.02 | 1320.00 | 0.0002 |
263.02 | 1330.00 | 0.0002 |
263.02 | 1970.00 | 0.0002 |
263.02 | 1980.00 | 0.0002 |
263.02 | 1990.00 | 0.0002 |
263.02 | 2010.00 | 0.0002 |
263.02 | 2020.00 | 0.0002 |
263.02 | 3420.00 | 0.0002 |
263.02 | 3430.00 | 0.0002 |
263.02 | 3450.00 | 0.0002 |
263.02 | 3520.00 | 0.0002 |
263.02 | 3560.00 | 0.0002 |
263.02 | 3590.00 | 0.0002 |
263.02 | 3640.00 | 0.0002 |
263.02 | 3670.00 | 0.0002 |
263.02 | 4800.00 | 0.0002 |
263.02 | 4840.00 | 0.0002 |
263.02 | 4870.00 | 0.0002 |
263.02 | 4910.00 | 0.0002 |
263.02 | 4950.00 | 0.0002 |
263.02 | 6990.00 | 0.0002 |
263.02 | 7090.00 | 0.0002 |
263.02 | 7160.00 | 0.0002 |
263.02 | 7200.00 | 0.0002 |
263.02 | 7230.00 | 0.0002 |
263.02 | 7310.00 | 0.0002 |
263.02 | 7380.00 | 0.0002 |
263.02 | 7390.00 | 0.0002 |
263.02 | 7420.00 | 0.0002 |
263.02 | 7460.00 | 0.0002 |
263.02 | 7520.00 | 0.0002 |
263.02 | 1320.00 | 0.0002 |
263.02 | 1330.00 | 0.0002 |
263.02 | 2020.00 | 0.0002 |
263.02 | 3670.00 | 0.0002 |
263.02 | 7310.00 | 0.0002 |
263.02 | 7460.00 | 0.0002 |
263.02 | 1330.00 | 0.0002 |
273.21 | 1420.00 | 0.0002 |
273.21 | 1430.00 | 0.0002 |
273.21 | 1440.00 | 0.0002 |
273.21 | 1450.00 | 0.0002 |
273.21 | 1810.00 | 0.0002 |
273.21 | 1820.00 | 0.0002 |
273.21 | 1860.00 | 0.0002 |
273.21 | 1890.00 | 0.0002 |
273.21 | 3450.00 | 0.0002 |
273.21 | 3460.00 | 0.0002 |
273.21 | 3490.00 | 0.0002 |
273.21 | 3500.00 | 0.0002 |
273.21 | 4850.00 | 0.0002 |
273.21 | 4860.00 | 0.0002 |
273.21 | 4880.00 | 0.0002 |
273.21 | 4910.00 | 0.0002 |
273.21 | 4960.00 | 0.0002 |
273.21 | 5010.00 | 0.0002 |
273.21 | 5030.00 | 0.0002 |
273.21 | 7780.00 | 0.0002 |
273.21 | 7800.00 | 0.0002 |
273.21 | 7810.00 | 0.0002 |
273.21 | 7900.00 | 0.0002 |
273.21 | 7960.00 | 0.0002 |
273.21 | 9530.00 | 0.0002 |
273.21 | 9540.00 | 0.0002 |
273.21 | 9580.00 | 0.0002 |
273.21 | 9610.00 | 0.0002 |
273.21 | 9770.00 | 0.0002 |
273.21 | 9880.00 | 0.0002 |
273.21 | 1440.00 | 0.0002 |
273.21 | 3450.00 | 0.0002 |
273.21 | 3490.00 | 0.0002 |
273.21 | 4880.00 | 0.0002 |
273.21 | 3450.00 | 0.0002 |
283.22 | 1240.00 | 0.0001 |
283.22 | 1260.00 | 0.0001 |
283.22 | 1470.00 | 0.0001 |
283.22 | 1510.00 | 0.0001 |
283.22 | 1530.00 | 0.0001 |
283.22 | 1570.00 | 0.0001 |
283.22 | 1900.00 | 0.0001 |
283.22 | 1930.00 | 0.0001 |
283.22 | 1950.00 | 0.0001 |
283.22 | 1970.00 | 0.0001 |
283.22 | 2000.00 | 0.0001 |
283.22 | 2050.00 | 0.0001 |
283.22 | 3700.00 | 0.0001 |
283.22 | 3720.00 | 0.0001 |
283.22 | 3850.00 | 0.0001 |
283.22 | 5130.00 | 0.0002 |
283.22 | 5220.00 | 0.0002 |
283.22 | 5260.00 | 0.0002 |
283.22 | 7400.00 | 0.0002 |
283.22 | 7500.00 | 0.0002 |
283.22 | 7540.00 | 0.0002 |
283.22 | 9720.00 | 0.0002 |
283.22 | 9780.00 | 0.0002 |
283.22 | 9940.00 | 0.0002 |
283.22 | 10050.00 | 0.0002 |
283.22 | 1240.00 | 0.0001 |
283.22 | 3700.00 | 0.0001 |
283.22 | 5260.00 | 0.0002 |
293.17 | 1370.00 | 0.0001 |
293.17 | 1390.00 | 0.0001 |
293.17 | 1400.00 | 0.0001 |
293.17 | 1420.00 | 0.0001 |
293.17 | 1430.00 | 0.0001 |
293.17 | 1440.00 | 0.0001 |
293.17 | 1850.00 | 0.0001 |
293.17 | 1860.00 | 0.0001 |
293.17 | 1890.00 | 0.0001 |
293.17 | 1920.00 | 0.0001 |
293.17 | 1940.00 | 0.0001 |
293.17 | 3820.00 | 0.0001 |
293.17 | 3830.00 | 0.0001 |
293.17 | 3850.00 | 0.0001 |
293.17 | 3860.00 | 0.0001 |
293.17 | 3870.00 | 0.0001 |
293.17 | 3890.00 | 0.0001 |
293.17 | 4900.00 | 0.0001 |
293.17 | 4920.00 | 0.0001 |
293.17 | 4960.00 | 0.0001 |
293.17 | 4970.00 | 0.0001 |
293.17 | 5010.00 | 0.0001 |
293.17 | 7450.00 | 0.0001 |
293.17 | 7490.00 | 0.0001 |
293.17 | 7520.00 | 0.0001 |
293.17 | 7550.00 | 0.0001 |
293.17 | 7560.00 | 0.0001 |
293.17 | 7590.00 | 0.0001 |
293.17 | 7620.00 | 0.0001 |
293.17 | 9740.00 | 0.0002 |
293.17 | 9770.00 | 0.0002 |
293.17 | 9820.00 | 0.0002 |
293.17 | 9880.00 | 0.0002 |
293.17 | 9970.00 | 0.0002 |
293.17 | 10070.00 | 0.0002 |
293.17 | 1390.00 | 0.0001 |
293.17 | 1430.00 | 0.0001 |
293.17 | 3890.00 | 0.0001 |
293.17 | 3890.00 | 0.0001 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Gas | Pressure, kPa - Gas | Mass density, kg/m3 - Gas |
283.15 | 203.60 | 7.588 |
283.15 | 399.90 | 15.605 |
283.15 | 505.80 | 20.282 |
283.15 | 605.00 | 24.932 |
283.15 | 651.60 | 27.227 |
283.15 | 651.70 | 27.238 |
283.15 | 700.80 | 29.728 |
283.15 | 750.80 | 32.361 |
283.15 | 781.50 | 34.03 |
283.15 | 781.60 | 34.039 |
283.15 | 801.70 | 35.15 |
283.15 | 801.80 | 35.164 |
283.15 | 820.20 | 36.196 |
283.15 | 820.30 | 36.205 |
283.15 | 203.60 | 7.589 |
283.15 | 399.90 | 15.605 |
283.15 | 505.80 | 20.278 |
283.15 | 605.00 | 24.935 |
283.15 | 700.80 | 29.729 |
283.15 | 750.80 | 32.363 |
293.15 | 201.70 | 7.219 |
293.15 | 201.80 | 7.222 |
293.15 | 400.30 | 14.916 |
293.15 | 599.30 | 23.356 |
293.15 | 701.30 | 28.031 |
293.15 | 798.20 | 32.729 |
293.15 | 898.70 | 37.925 |
293.15 | 951.00 | 40.774 |
293.15 | 999.60 | 43.532 |
293.15 | 1030.90 | 45.365 |
293.15 | 1048.70 | 46.429 |
293.15 | 1048.80 | 46.429 |
293.15 | 1071.00 | 47.788 |
293.15 | 1071.10 | 47.784 |
293.15 | 1089.00 | 48.896 |
293.15 | 400.30 | 14.915 |
293.15 | 599.30 | 23.36 |
293.15 | 701.30 | 28.028 |
293.15 | 798.20 | 32.732 |
293.15 | 898.70 | 37.921 |
293.15 | 951.00 | 40.774 |
293.15 | 999.60 | 43.532 |
293.15 | 1030.90 | 45.355 |
293.15 | 1089.00 | 48.901 |
303.15 | 200.00 | 6.895 |
303.15 | 400.90 | 14.305 |
303.15 | 600.30 | 22.265 |
303.15 | 600.40 | 22.265 |
303.15 | 801.60 | 31.034 |
303.15 | 1001.00 | 40.662 |
303.15 | 1099.90 | 45.879 |
303.15 | 1197.30 | 51.364 |
303.15 | 1249.20 | 54.458 |
303.15 | 1299.50 | 57.578 |
303.15 | 1340.60 | 60.231 |
303.15 | 1369.80 | 62.181 |
303.15 | 1401.50 | 64.363 |
303.15 | 1423.70 | 65.925 |
303.15 | 1423.90 | 65.952 |
303.15 | 200.00 | 6.903 |
303.15 | 400.90 | 14.313 |
303.15 | 801.60 | 31.031 |
303.15 | 1001.00 | 40.666 |
303.15 | 1099.90 | 45.88 |
303.15 | 1197.30 | 51.363 |
303.15 | 1299.50 | 57.581 |
303.15 | 1340.60 | 60.229 |
303.15 | 1369.80 | 62.183 |
303.15 | 1401.50 | 64.364 |
313.15 | 201.50 | 6.696 |
313.15 | 201.80 | 6.718 |
313.15 | 205.10 | 6.831 |
313.15 | 206.20 | 6.869 |
313.15 | 401.60 | 13.776 |
313.15 | 401.70 | 13.775 |
313.15 | 600.30 | 21.275 |
313.15 | 800.30 | 29.41 |
313.15 | 999.10 | 38.197 |
313.15 | 1200.30 | 47.988 |
313.15 | 1400.20 | 58.893 |
313.15 | 1500.80 | 64.963 |
313.15 | 1540.90 | 67.443 |
313.15 | 1598.00 | 71.29 |
313.15 | 1598.10 | 71.312 |
313.15 | 1648.30 | 74.652 |
313.15 | 1701.30 | 78.498 |
313.15 | 1740.80 | 81.508 |
313.15 | 1771.10 | 83.908 |
313.15 | 1793.20 | 85.73 |
313.15 | 1794.40 | 85.811 |
313.15 | 205.10 | 6.828 |
313.15 | 600.30 | 21.282 |
313.15 | 800.30 | 29.413 |
313.15 | 999.10 | 38.204 |
313.15 | 1200.30 | 48.002 |
313.15 | 1400.20 | 58.909 |
313.15 | 1500.80 | 64.977 |
313.15 | 1540.90 | 67.442 |
313.15 | 1648.30 | 74.647 |
313.15 | 1701.30 | 78.51 |
313.15 | 1740.80 | 81.517 |
313.15 | 1771.10 | 83.916 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.19; 3729.50] | kPa | [161.82; 345.86] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43786e+01 | |||
Coefficient B | -1.99833e+03 | |||
Coefficient C | -2.11680e+01 | |||
Temperature range, min. | 161.82 | |||
Temperature range, max. | 345.86 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 250 300 350 | ||||
Pvap | 1.19 | kPa | 161.82 | Calculated Property |
Pvap | 7.20 | kPa | 182.27 | Calculated Property |
Pvap | 29.12 | kPa | 202.72 | Calculated Property |
Pvap | 88.75 | kPa | 223.17 | Calculated Property |
Pvap | 220.34 | kPa | 243.62 | Calculated Property |
Pvap | 469.41 | kPa | 264.06 | Calculated Property |
Pvap | 889.20 | kPa | 284.51 | Calculated Property |
Pvap | 1536.24 | kPa | 304.96 | Calculated Property |
Pvap | 2466.04 | kPa | 325.41 | Calculated Property |
Pvap | 3729.50 | kPa | 345.86 | Calculated Property |
Pvap | [1.14; 3748.81] | kPa | [161.85; 346.25] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.77777e+01 | |||
Coefficient B | -3.95200e+03 | |||
Coefficient C | -8.58781e+00 | |||
Coefficient D | 1.73454e-05 | |||
Temperature range, min. | 161.85 | |||
Temperature range, max. | 346.25 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 250 300 350 | ||||
Pvap | 1.14 | kPa | 161.85 | Calculated Property |
Pvap | 7.20 | kPa | 182.34 | Calculated Property |
Pvap | 29.53 | kPa | 202.83 | Calculated Property |
Pvap | 89.83 | kPa | 223.32 | Calculated Property |
Pvap | 220.81 | kPa | 243.81 | Calculated Property |
Pvap | 464.76 | kPa | 264.29 | Calculated Property |
Pvap | 872.40 | kPa | 284.78 | Calculated Property |
Pvap | 1503.72 | kPa | 305.27 | Calculated Property |
Pvap | 2431.66 | kPa | 325.76 | Calculated Property |
Pvap | 3748.81 | kPa | 346.25 | Calculated Property |
Find more compounds similar to Ethane, 1,1,1-trifluoro-.
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