Property | Value | Unit | Source |
---|---|---|---|
PAff | 888.50 | kJ/mol | NIST |
BasG | 857.60 | kJ/mol | NIST |
ΔcH°liquid | -1867.70 ± 1.30 | kJ/mol | NIST |
ΔcH°solid | -1862.10 ± 5.10 | kJ/mol | NIST |
ΔfG° | -65.15 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -248.00 ± 5.50 | kJ/mol | NIST |
ΔfH°liquid | -313.20 ± 1.30 | kJ/mol | NIST |
ΔfH°solid | -318.80 ± 5.10 | kJ/mol | NIST |
ΔfusH° | 10.22 | kJ/mol | Joback Calculated Property |
ΔsubH° | [69.87; 70.80] | kJ/mol |
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ΔsubH° | 70.80 ± 2.00 | kJ/mol | NIST |
ΔsubH° | 70.80 ± 2.00 | kJ/mol | NIST |
ΔsubH° | 69.87 ± 0.31 | kJ/mol | NIST |
ΔvapH° | 35.45 | kJ/mol | Joback Calculated Property |
IE | [8.90; 9.85] | eV |
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IE | 9.70 ± 0.05 | eV | NIST |
IE | 8.90 ± 0.02 | eV | NIST |
IE | 9.85 | eV | NIST |
log10WS | -0.04 | Crippen Calculated Property | |
logPoct/wat | -0.248 | Crippen Calculated Property | |
McVol | 64.680 | ml/mol | McGowan Calculated Property |
Pc | 4890.21 | kPa | Joback Calculated Property |
Inp | [825.00; 857.00] |
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|
Inp | 857.00 | NIST | |
Inp | 825.00 | NIST | |
I | [1609.00; 1648.00] |
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|
I | 1623.00 | NIST | |
I | 1623.00 | NIST | |
I | 1609.00 | NIST | |
I | 1648.00 | NIST | |
I | 1609.00 | NIST | |
Tboil | [478.07; 479.15] | K |
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Tboil | 478.07 | K | Isobari... |
Tboil | 479.15 | K | Vapor-L... |
Tboil | 478.20 | K | NIST |
Tc | 557.68 | K | Joback Calculated Property |
Tfus | [302.90; 303.67] | K |
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Tfus | 303.43 ± 0.20 | K | NIST |
Tfus | 302.90 ± 1.00 | K | NIST |
Tfus | 303.67 ± 0.15 | K | NIST |
Vc | 0.244 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [109.61; 146.12] | J/mol×K | [372.08; 557.68] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 115 120 125 130 135 140 145 400 450 500 550 | ||||
Cp,gas | 109.61 | J/mol×K | 372.08 | Joback Calculated Property |
Cp,gas | 116.34 | J/mol×K | 403.01 | Joback Calculated Property |
Cp,gas | 122.81 | J/mol×K | 433.95 | Joback Calculated Property |
Cp,gas | 129.01 | J/mol×K | 464.88 | Joback Calculated Property |
Cp,gas | 134.96 | J/mol×K | 495.81 | Joback Calculated Property |
Cp,gas | 140.66 | J/mol×K | 526.75 | Joback Calculated Property |
Cp,gas | 146.12 | J/mol×K | 557.68 | Joback Calculated Property |
η | [0.0026072; 0.0038224] | Pa×s | [303.15; 318.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.60e-3 2.80e-3 3.00e-3 3.20e-3 3.40e-3 3.60e-3 3.80e-3 305 310 315 | ||||
η | 0.0038224 | Pa×s | 303.15 | Volumet... |
η | 0.0038224 | Pa×s | 303.15 | Volumet... |
η | 0.0033124 | Pa×s | 308.15 | Volumet... |
η | 0.0029041 | Pa×s | 313.15 | Volumet... |
η | 0.0026072 | Pa×s | 318.15 | Volumet... |
ΔfusH | [9.73; 10.11] | kJ/mol | [303.70; 303.80] | ![]() |
ΔfusH | 10.11 | kJ/mol | 303.70 | NIST |
ΔfusH | 9.73 | kJ/mol | 303.80 | NIST |
ΔfusH | 9.73 | kJ/mol | 303.80 | NIST |
ΔsubH | 54.00 | kJ/mol | 295.50 | NIST |
ΔvapH | [53.50; 62.00] | kJ/mol | [388.00; 416.00] | ![]() |
ΔvapH | 59.60 | kJ/mol | 388.00 | NIST |
ΔvapH | 55.50 | kJ/mol | 388.50 | NIST |
ΔvapH | 62.00 | kJ/mol | 390.50 | NIST |
ΔvapH | 53.50 | kJ/mol | 416.00 | NIST |
ρl | [928.93; 958.40] | kg/m3 | [293.15; 328.15] | ![]() |
T(K) Liquid Density (kg/m3) 930 935 940 945 950 955 960 300 310 320 | ||||
ρl | 956.30 | kg/m3 | 293.15 | Interpr... |
ρl | 958.40 | kg/m3 | 293.15 | Densiti... |
ρl | 954.20 | kg/m3 | 298.15 | Densiti... |
ρl | 951.20 | kg/m3 | 298.15 | Interpr... |
ρl | 950.20 | kg/m3 | 303.15 | Interpr... |
ρl | 950.10 | kg/m3 | 303.15 | Densiti... |
ρl | 946.80 | kg/m3 | 308.15 | Interpr... |
ρl | 945.85 | kg/m3 | 308.15 | Density... |
ρl | 945.90 | kg/m3 | 308.15 | Densiti... |
ρl | 946.01 | kg/m3 | 308.15 | Density... |
ρl | 945.71 | kg/m3 | 308.15 | Density... |
ρl | 949.70 | kg/m3 | 308.15 | Ultraso... |
ρl | 940.50 | kg/m3 | 313.15 | Interpr... |
ρl | 941.63 | kg/m3 | 313.15 | Density... |
ρl | 941.53 | kg/m3 | 313.15 | Density... |
ρl | 941.70 | kg/m3 | 313.15 | Densiti... |
ρl | 941.81 | kg/m3 | 313.15 | Density... |
ρl | 937.33 | kg/m3 | 318.15 | Density... |
ρl | 937.59 | kg/m3 | 318.15 | Density... |
ρl | 937.60 | kg/m3 | 318.15 | Densiti... |
ρl | 937.44 | kg/m3 | 318.15 | Density... |
ρl | 933.24 | kg/m3 | 323.15 | Density... |
ρl | 933.16 | kg/m3 | 323.15 | Density... |
ρl | 933.36 | kg/m3 | 323.15 | Density... |
ρl | 929.17 | kg/m3 | 328.15 | Density... |
ρl | 929.07 | kg/m3 | 328.15 | Density... |
ρl | 928.93 | kg/m3 | 328.15 | Density... |
csound,fluid | [1319.00; 1367.00] | m/s | [303.15; 318.15] | ![]() |
csound,fluid | 1367.00 | m/s | 303.15 | Density... |
csound,fluid | 1362.00 | m/s | 308.15 | Density... |
csound,fluid | 1334.00 | m/s | 313.15 | Density... |
csound,fluid | 1319.00 | m/s | 318.15 | Density... |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
308.15 | 101.30 | 0.0033 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
308.15 | 101.00 | 0.0033 |
Reference |
Fixed | Measured | |
---|---|---|
Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
101.30 | 308.15 | 0.0037 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [359.94; 506.89] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50574e+01 | |||
Coefficient B | -4.21034e+03 | |||
Coefficient C | -7.48750e+01 | |||
Temperature range, min. | 359.94 | |||
Temperature range, max. | 506.89 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 359.94 | Calculated Property |
Pvap | 2.97 | kPa | 376.27 | Calculated Property |
Pvap | 6.08 | kPa | 392.60 | Calculated Property |
Pvap | 11.63 | kPa | 408.92 | Calculated Property |
Pvap | 20.92 | kPa | 425.25 | Calculated Property |
Pvap | 35.72 | kPa | 441.58 | Calculated Property |
Pvap | 58.28 | kPa | 457.91 | Calculated Property |
Pvap | 91.35 | kPa | 474.23 | Calculated Property |
Pvap | 138.21 | kPa | 490.56 | Calculated Property |
Pvap | 202.67 | kPa | 506.89 | Calculated Property |
Pvap | [0.03; 4741.51] | kPa | [301.15; 718.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.63193e+01 | |||
Coefficient B | -8.67256e+03 | |||
Coefficient C | -5.45449e+00 | |||
Coefficient D | 1.83955e-07 | |||
Temperature range, min. | 301.15 | |||
Temperature range, max. | 718.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 400 600 | ||||
Pvap | 0.03 | kPa | 301.15 | Calculated Property |
Pvap | 0.59 | kPa | 347.47 | Calculated Property |
Pvap | 5.64 | kPa | 393.78 | Calculated Property |
Pvap | 31.42 | kPa | 440.10 | Calculated Property |
Pvap | 119.83 | kPa | 486.42 | Calculated Property |
Pvap | 346.81 | kPa | 532.73 | Calculated Property |
Pvap | 817.02 | kPa | 579.05 | Calculated Property |
Pvap | 1644.96 | kPa | 625.37 | Calculated Property |
Pvap | 2930.96 | kPa | 671.68 | Calculated Property |
Pvap | 4741.51 | kPa | 718.00 | Calculated Property |
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