| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5599 | Relay (1.0) Calculated Property | |
| ΔfG° | -261.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -427.40 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 7.87 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.81 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.05 | eV | Relay (1.0) Calculated Property |
| log10WS | 1.03 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.014 | Crippen Calculated Property | |
| McVol | 78.960 | ml/mol | McGowan Calculated Property |
| Pc | 4333.96 | kPa | Joback Calculated Property |
| Inp | [661.00; 669.00] |
|
|
| Inp | 661.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 669.00 | NIST | |
| Tboil | 402.65 | K | Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa |
| Tc | 596.60 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tfus | 192.32 | K | Relay (1.0) Calculated Property |
| Vc | 0.281 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [154.76; 194.69] | J/mol×K | [405.28; 571.50] | |
| Cp,gas | 154.76 | J/mol×K | 405.28 | Joback Calculated Property |
| Cp,gas | 161.91 | J/mol×K | 432.98 | Joback Calculated Property |
| Cp,gas | 168.86 | J/mol×K | 460.69 | Joback Calculated Property |
| Cp,gas | 175.62 | J/mol×K | 488.39 | Joback Calculated Property |
| Cp,gas | 182.18 | J/mol×K | 516.09 | Joback Calculated Property |
| Cp,gas | 188.54 | J/mol×K | 543.79 | Joback Calculated Property |
| Cp,gas | 194.69 | J/mol×K | 571.50 | Joback Calculated Property |
| η | [0.0002584; 0.1431690] | Pa×s | [202.89; 405.28] | |
| η | 0.1431690 | Pa×s | 202.89 | Joback Calculated Property |
| η | 0.0235868 | Pa×s | 236.62 | Joback Calculated Property |
| η | 0.0060943 | Pa×s | 270.35 | Joback Calculated Property |
| η | 0.0021260 | Pa×s | 304.08 | Joback Calculated Property |
| η | 0.0009153 | Pa×s | 337.82 | Joback Calculated Property |
| η | 0.0004592 | Pa×s | 371.55 | Joback Calculated Property |
| η | 0.0002584 | Pa×s | 405.28 | Joback Calculated Property |
| Pvap | 101.30 | kPa | 402.65 | Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.61] | kPa | [308.22; 389.69] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.10436e+01 | |||
| Coefficient B | -5.29554e+03 | |||
| Coefficient C | -5.30870e+01 | |||
| Temperature range, min. | 308.22 | |||
| Temperature range, max. | 389.69 | |||
| Pvap | 1.33 | kPa | 308.22 | Calculated Property |
| Pvap | 2.71 | kPa | 317.27 | Calculated Property |
| Pvap | 5.27 | kPa | 326.32 | Calculated Property |
| Pvap | 9.82 | kPa | 335.38 | Calculated Property |
| Pvap | 17.59 | kPa | 344.43 | Calculated Property |
| Pvap | 30.41 | kPa | 353.48 | Calculated Property |
| Pvap | 50.94 | kPa | 362.53 | Calculated Property |
| Pvap | 82.85 | kPa | 371.59 | Calculated Property |
| Pvap | 131.17 | kPa | 380.64 | Calculated Property |
| Pvap | 202.61 | kPa | 389.69 | Calculated Property |
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