Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -1504.20 ± 0.92 | kJ/mol | NIST |
ΔfG° | -619.14 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -718.07 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | -799.31 ± 0.92 | kJ/mol | NIST |
ΔfusH° | 9.55 | kJ/mol | Joback Calculated Property |
ΔvapH° | 22.91 | kJ/mol | Joback Calculated Property |
log10WS | -1.89 | Crippen Calculated Property | |
logPoct/wat | 2.178 | Crippen Calculated Property | |
McVol | 70.680 | ml/mol | McGowan Calculated Property |
Pc | 3633.35 | kPa | Joback Calculated Property |
S°liquid | [271.67; 271.67] | J/mol×K |
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S°liquid | 271.67 | J/mol×K | NIST |
S°liquid | 271.67 | J/mol×K | NIST |
Tboil | 319.00 | K | NIST |
Tc | 453.65 | K | Joback Calculated Property |
Tfus | 157.68 | K | Joback Calculated Property |
Ttriple | [179.32; 179.40] | K |
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Ttriple | 179.32 ± 0.02 | K | NIST |
Ttriple | 179.40 ± 0.02 | K | NIST |
Vc | 0.295 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [112.93; 147.12] | J/mol×K | [300.05; 453.65] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 150 300 350 400 450 | ||||
Cp,gas | 112.93 | J/mol×K | 300.05 | Joback Calculated Property |
Cp,gas | 119.45 | J/mol×K | 325.65 | Joback Calculated Property |
Cp,gas | 125.62 | J/mol×K | 351.25 | Joback Calculated Property |
Cp,gas | 131.46 | J/mol×K | 376.85 | Joback Calculated Property |
Cp,gas | 136.98 | J/mol×K | 402.45 | Joback Calculated Property |
Cp,gas | 142.20 | J/mol×K | 428.05 | Joback Calculated Property |
Cp,gas | 147.12 | J/mol×K | 453.65 | Joback Calculated Property |
Cp,liquid | [171.08; 171.08] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 171.08 | J/mol×K | 298.15 | NIST |
Cp,liquid | 171.08 | J/mol×K | 298.15 | NIST |
ΔfusH | [4.49; 5.31] | kJ/mol | [169.80; 179.40] | ![]() |
ΔfusH | 4.49 | kJ/mol | 169.80 | NIST |
ΔfusH | 5.05 | kJ/mol | 179.30 | NIST |
ΔfusH | 5.31 | kJ/mol | 179.40 | NIST |
ΔvapH | [29.90; 33.70] | kJ/mol | [306.00; 321.00] | ![]() |
ΔvapH | 29.90 | kJ/mol | 306.00 | NIST |
ΔvapH | 33.70 | kJ/mol | 321.00 | NIST |
ΔfusS | [26.44; 28.20] | J/mol×K | [169.80; 179.30] | ![]() |
ΔfusS | 26.44 | J/mol×K | 169.80 | NIST |
ΔfusS | 28.20 | J/mol×K | 179.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [233.90; 340.61] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.38810e+01 | |||
Coefficient B | -2.47417e+03 | |||
Coefficient C | -5.18870e+01 | |||
Temperature range, min. | 233.90 | |||
Temperature range, max. | 340.61 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 1.33 | kPa | 233.90 | Calculated Property |
Pvap | 3.06 | kPa | 245.76 | Calculated Property |
Pvap | 6.39 | kPa | 257.61 | Calculated Property |
Pvap | 12.30 | kPa | 269.47 | Calculated Property |
Pvap | 22.14 | kPa | 281.33 | Calculated Property |
Pvap | 37.61 | kPa | 293.18 | Calculated Property |
Pvap | 60.80 | kPa | 305.04 | Calculated Property |
Pvap | 94.14 | kPa | 316.90 | Calculated Property |
Pvap | 140.42 | kPa | 328.75 | Calculated Property |
Pvap | 202.67 | kPa | 340.61 | Calculated Property |
Find more compounds similar to Propane, 3-chloro-1,1,1-trifluoro-.
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