Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -221.55 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -405.31 | kJ/mol | Joback Calculated Property |
ΔfusH° | 23.55 | kJ/mol | Heat ca... |
ΔvapH° | 67.20 | kJ/mol | Joback Calculated Property |
log10WS | 0.43 | Crippen Calculated Property | |
logPoct/wat | -1.312 | Crippen Calculated Property | |
McVol | 88.940 | ml/mol | McGowan Calculated Property |
Pc | 5552.58 | kPa | Joback Calculated Property |
Tboil | 544.58 | K | Joback Calculated Property |
Tc | 722.63 | K | Joback Calculated Property |
Tfus | 384.00 ± 2.00 | K | NIST |
Ttriple | 384.08 ± 0.05 | K | NIST |
Vc | 0.316 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [223.23; 261.08] | J/mol×K | [544.58; 722.63] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 550 600 650 700 | ||||
Cp,gas | 223.23 | J/mol×K | 544.58 | Joback Calculated Property |
Cp,gas | 230.48 | J/mol×K | 574.26 | Joback Calculated Property |
Cp,gas | 237.32 | J/mol×K | 603.93 | Joback Calculated Property |
Cp,gas | 243.78 | J/mol×K | 633.61 | Joback Calculated Property |
Cp,gas | 249.88 | J/mol×K | 663.28 | Joback Calculated Property |
Cp,gas | 255.64 | J/mol×K | 692.96 | Joback Calculated Property |
Cp,gas | 261.08 | J/mol×K | 722.63 | Joback Calculated Property |
Cp,solid | 161.37 | J/mol×K | 301.40 | NIST |
ΔfusH | [2.73; 25.21] | kJ/mol | [338.00; 384.10] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 5 10 15 20 25 340 360 380 | ||||
ΔfusH | 2.78 | kJ/mol | 338.00 | NIST |
ΔfusH | 24.68 | kJ/mol | 351.30 | NIST |
ΔfusH | 25.21 | kJ/mol | 352.00 | NIST |
ΔfusH | 5.00 | kJ/mol | 352.90 | NIST |
ΔfusH | 18.46 | kJ/mol | 353.70 | NIST |
ΔfusH | 2.73 | kJ/mol | 383.60 | NIST |
ΔfusH | 2.99 | kJ/mol | 384.00 | NIST |
ΔfusH | 2.99 | kJ/mol | 384.00 | NIST |
ΔfusH | 2.76 | kJ/mol | 384.10 | NIST |
ΔfusH | 2.78 | kJ/mol | 384.10 | NIST |
ΔfusS | [7.12; 71.61] | J/mol×K | [351.30; 384.10] | ![]() |
T(K) Entropy of fusion at a given temperature (J/mol×K) 10 20 30 40 50 60 70 360 370 380 | ||||
ΔfusS | 70.26 | J/mol×K | 351.30 | NIST |
ΔfusS | 71.61 | J/mol×K | 352.00 | NIST |
ΔfusS | 14.17 | J/mol×K | 352.90 | NIST |
ΔfusS | 52.19 | J/mol×K | 353.70 | NIST |
ΔfusS | 7.12 | J/mol×K | 383.60 | NIST |
ΔfusS | 7.79 | J/mol×K | 384.00 | NIST |
ΔfusS | 7.24 | J/mol×K | 384.10 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 424.70 | K | 1.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.60] | kPa | [420.32; 467.63] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 4.06801e+01 | |||
Coefficient B | -1.34550e+04 | |||
Coefficient C | -8.72100e+01 | |||
Temperature range, min. | 420.32 | |||
Temperature range, max. | 467.63 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 420 440 460 | ||||
Pvap | 1.33 | kPa | 420.32 | Calculated Property |
Pvap | 2.50 | kPa | 425.58 | Calculated Property |
Pvap | 4.59 | kPa | 430.83 | Calculated Property |
Pvap | 8.28 | kPa | 436.09 | Calculated Property |
Pvap | 14.68 | kPa | 441.35 | Calculated Property |
Pvap | 25.58 | kPa | 446.60 | Calculated Property |
Pvap | 43.89 | kPa | 451.86 | Calculated Property |
Pvap | 74.14 | kPa | 457.12 | Calculated Property |
Pvap | 123.43 | kPa | 462.37 | Calculated Property |
Pvap | 202.60 | kPa | 467.63 | Calculated Property |
Find more compounds similar to 2-Amino-2-methyl-1,3-propanediol.
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