| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4200 | Relay (1.0) Calculated Property | |
| ΔfG° | -210.36 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -436.40 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 13.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 39.56 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.56 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.79 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.407 | Crippen Calculated Property | |
| McVol | 107.140 | ml/mol | McGowan Calculated Property |
| Pc | 2992.59 | kPa | Joback Calculated Property |
| Inp | [731.00; 735.00] |
|
|
| Inp | 731.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 731.00 | NIST | |
| Tboil | 380.52 | K | Relay (1.0) Calculated Property |
| Tc | 553.75 | K | Relay (1.0) Calculated Property |
| Tfus | 176.47 | K | Relay (1.0) Calculated Property |
| Vc | 0.412 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [831.10; 831.40] | kg/m3 | [293.15; 293.15] | |
| ρl | 831.40 | kg/m3 | 293.15 | Measurement and correlation of (vapour-liquid) equilibrium for binary mixtures composed of 1-(ethoxymethoxy)-propane with ethanol and 1-propanol at 101.33 kPa |
| ρl | 831.10 | kg/m3 | 293.15 | Three Binary Azeotropic Systems for 1-(Methoxymethoxy)-propane, 1-(Ethoxymethoxy)-propane, and Methoxy(methoxymethoxy)methane with Three Alcohols at 101.33 kPa: Experimental Data, Correlation, and Purification |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [163.57; 365.87] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.84340e+01 | |||
| Coefficient B | 4.47440e-01 | |||
| Coefficient C | -8.06000e-05 | |||
| Coefficient D | -4.94000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 163.57 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 194.45 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 223.60 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 250.85 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 276.05 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 299.05 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 319.69 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 337.81 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 353.26 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 365.87 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0027699; 0.0002010] | Pa×s | [201.84; 382.97] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.14358e+01 | |||
| Coefficient B | 1.11958e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 201.84 | |||
| Temperature range, max. | 382.97 | |||
| η | 0.0027699 | Pa×s | 201.84 | Calculated Property |
| η | 0.0016751 | Pa×s | 221.97 | Calculated Property |
| η | 0.0011014 | Pa×s | 242.09 | Calculated Property |
| η | 0.0007723 | Pa×s | 262.22 | Calculated Property |
| η | 0.0005696 | Pa×s | 282.34 | Calculated Property |
| η | 0.0004375 | Pa×s | 302.47 | Calculated Property |
| η | 0.0003473 | Pa×s | 322.59 | Calculated Property |
| η | 0.0002833 | Pa×s | 342.72 | Calculated Property |
| η | 0.0002363 | Pa×s | 362.85 | Calculated Property |
| η | 0.0002010 | Pa×s | 382.97 | Calculated Property |
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