Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -37.26 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -236.51 | kJ/mol | Joback Calculated Property |
ΔfusH° | 12.29 | kJ/mol | Joback Calculated Property |
ΔvapH° | 45.06 | kJ/mol | Joback Calculated Property |
log10WS | 0.14 | Crippen Calculated Property | |
logPoct/wat | -0.071 | Crippen Calculated Property | |
McVol | 97.160 | ml/mol | McGowan Calculated Property |
Pc | 3906.25 | kPa | Joback Calculated Property |
Tboil | 397.20 | K | NIST |
Tc | 581.92 | K | Joback Calculated Property |
Tfus | 224.40 | K | Joback Calculated Property |
Vc | 0.346 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [197.91; 250.40] | J/mol×K | [417.98; 581.92] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 200 210 220 230 240 250 450 500 550 | ||||
Cp,gas | 197.91 | J/mol×K | 417.98 | Joback Calculated Property |
Cp,gas | 207.62 | J/mol×K | 445.30 | Joback Calculated Property |
Cp,gas | 216.93 | J/mol×K | 472.63 | Joback Calculated Property |
Cp,gas | 225.85 | J/mol×K | 499.95 | Joback Calculated Property |
Cp,gas | 234.40 | J/mol×K | 527.28 | Joback Calculated Property |
Cp,gas | 242.58 | J/mol×K | 554.60 | Joback Calculated Property |
Cp,gas | 250.40 | J/mol×K | 581.92 | Joback Calculated Property |
ρl | [820.90; 845.20] | kg/m3 | [298.15; 323.15] | ![]() |
T(K) Liquid Density (kg/m3) 820 825 830 835 840 845 300 310 320 | ||||
ρl | 845.20 | kg/m3 | 298.15 | Density... |
ρl | 840.40 | kg/m3 | 303.15 | Density... |
ρl | 835.60 | kg/m3 | 308.15 | Density... |
ρl | 830.70 | kg/m3 | 313.15 | Density... |
ρl | 825.90 | kg/m3 | 318.15 | Density... |
ρl | 820.90 | kg/m3 | 323.15 | Density... |
γ | [0.02; 0.02] | N/m | [303.20; 323.20] | ![]() |
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 305 310 315 320 | ||||
γ | 0.02 | N/m | 303.20 | Surface... |
γ | 0.02 | N/m | 303.20 | Analysi... |
γ | 0.02 | N/m | 308.20 | Analysi... |
γ | 0.02 | N/m | 313.20 | Surface... |
γ | 0.02 | N/m | 313.20 | Analysi... |
γ | 0.02 | N/m | 318.20 | Analysi... |
γ | 0.02 | N/m | 323.20 | Surface... |
γ | 0.02 | N/m | 323.20 | Analysi... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.32; 202.65] | kPa | [302.99; 419.21] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.61920e+01 | |||
Coefficient B | -3.99873e+03 | |||
Coefficient C | -5.16970e+01 | |||
Temperature range, min. | 302.99 | |||
Temperature range, max. | 419.21 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
Pvap | 1.32 | kPa | 302.99 | Calculated Property |
Pvap | 2.88 | kPa | 315.90 | Calculated Property |
Pvap | 5.83 | kPa | 328.82 | Calculated Property |
Pvap | 11.08 | kPa | 341.73 | Calculated Property |
Pvap | 19.94 | kPa | 354.64 | Calculated Property |
Pvap | 34.20 | kPa | 367.56 | Calculated Property |
Pvap | 56.23 | kPa | 380.47 | Calculated Property |
Pvap | 89.04 | kPa | 393.38 | Calculated Property |
Pvap | 136.35 | kPa | 406.30 | Calculated Property |
Pvap | 202.65 | kPa | 419.21 | Calculated Property |
Find more compounds similar to 2-Propanol, 1-(dimethylamino)-.
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