Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 14.90 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -31.54 | kJ/mol | Joback Calculated Property |
ΔfusH° | 15.86 | kJ/mol | Joback Calculated Property |
ΔvapH° | 41.19 | kJ/mol | Joback Calculated Property |
log10WS | -2.49 | Crippen Calculated Property | |
logPoct/wat | 2.540 | Crippen Calculated Property | |
McVol | 105.630 | ml/mol | McGowan Calculated Property |
Pc | 5999.95 | kPa | Joback Calculated Property |
Inp | 1148.00 | NIST | |
Tboil | [493.20; 495.30] | K |
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Tboil | 493.20 | K | NIST |
Tboil | 495.30 | K | NIST |
Tc | 699.87 | K | Joback Calculated Property |
Tfus | [285.41; 289.30] | K |
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Tfus | 289.30 ± 0.02 | K | NIST |
Tfus | 285.41 ± 0.05 | K | NIST |
Vc | 0.384 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [149.10; 178.04] | J/mol×K | [466.08; 699.87] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 150 155 160 165 170 175 180 500 600 700 | ||||
Cp,gas | 149.10 | J/mol×K | 466.08 | Joback Calculated Property |
Cp,gas | 155.03 | J/mol×K | 505.05 | Joback Calculated Property |
Cp,gas | 160.46 | J/mol×K | 544.01 | Joback Calculated Property |
Cp,gas | 165.43 | J/mol×K | 582.98 | Joback Calculated Property |
Cp,gas | 169.98 | J/mol×K | 621.94 | Joback Calculated Property |
Cp,gas | 174.17 | J/mol×K | 660.91 | Joback Calculated Property |
Cp,gas | 178.04 | J/mol×K | 699.87 | Joback Calculated Property |
Cp,liquid | 166.50 | J/mol×K | 298.00 | NIST |
η | [0.0004514; 0.0032395] | Pa×s | [287.97; 466.08] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 300 350 400 450 | ||||
η | 0.0032395 | Pa×s | 287.97 | Joback Calculated Property |
η | 0.0020007 | Pa×s | 317.66 | Joback Calculated Property |
η | 0.0013417 | Pa×s | 347.34 | Joback Calculated Property |
η | 0.0009582 | Pa×s | 377.02 | Joback Calculated Property |
η | 0.0007188 | Pa×s | 406.71 | Joback Calculated Property |
η | 0.0005607 | Pa×s | 436.39 | Joback Calculated Property |
η | 0.0004514 | Pa×s | 466.08 | Joback Calculated Property |
ΔfusH | [23.78; 23.78] | kJ/mol | [289.40; 289.40] | ![]() |
ΔfusH | 23.78 | kJ/mol | 289.40 | NIST |
ΔfusH | 23.78 | kJ/mol | 289.40 | NIST |
ΔvapH | [50.20; 50.80] | kJ/mol | [439.00; 492.50] | ![]() |
ΔvapH | 50.20 | kJ/mol | 439.00 | NIST |
ΔvapH | 50.80 | kJ/mol | 492.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 215.81] | kPa | [373.75; 524.73] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.53100e+01 | |||
Coefficient B | -4.43013e+03 | |||
Coefficient C | -7.88460e+01 | |||
Temperature range, min. | 373.75 | |||
Temperature range, max. | 524.73 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 373.75 | Calculated Property |
Pvap | 2.99 | kPa | 390.53 | Calculated Property |
Pvap | 6.19 | kPa | 407.30 | Calculated Property |
Pvap | 11.91 | kPa | 424.08 | Calculated Property |
Pvap | 21.59 | kPa | 440.85 | Calculated Property |
Pvap | 37.12 | kPa | 457.63 | Calculated Property |
Pvap | 60.96 | kPa | 474.40 | Calculated Property |
Pvap | 96.15 | kPa | 491.18 | Calculated Property |
Pvap | 146.35 | kPa | 507.95 | Calculated Property |
Pvap | 215.81 | kPa | 524.73 | Calculated Property |
Find more compounds similar to Propane, 1,2,3-tribromo-.
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