Property | Value | Unit | Source |
---|---|---|---|

Δ_{f}G° |
-293.28 | kJ/mol | Joback Calculated Property |

Δ_{f}H°_{gas} |
-435.63 | kJ/mol | Joback Calculated Property |

Δ_{fus}H° |
10.77 | kJ/mol | Joback Calculated Property |

Δ_{vap}H° |
[71.30; 73.60] | kJ/mol | |

Δ_{vap}H° |
73.60 ± 0.20 | kJ/mol | NIST |

Δ_{vap}H° |
71.30 ± 0.50 | kJ/mol | NIST |

log_{10}WS |
0.22 | Crippen Calculated Property | |

logP_{oct/wat} |
-0.393 | Crippen Calculated Property | |

McVol | 78.960 | ml/mol | McGowan Calculated Property |

P_{c} |
5029.93 | kPa | Joback Calculated Property |

T_{boil} |
474.84 | K | Joback Calculated Property |

T_{c} |
636.47 | K | Joback Calculated Property |

T_{fus} |
241.48 | K | Joback Calculated Property |

V_{c} |
0.291 | m^{3}/kmol |
Joback Calculated Property |

Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|

C_{p,gas} |
[173.31; 209.35] | J/mol×K | [474.84; 636.47] | |

C_{p,gas} |
173.31 | J/mol×K | 474.84 | Joback Calculated Property |

C_{p,gas} |
179.93 | J/mol×K | 501.78 | Joback Calculated Property |

C_{p,gas} |
186.29 | J/mol×K | 528.72 | Joback Calculated Property |

C_{p,gas} |
192.41 | J/mol×K | 555.66 | Joback Calculated Property |

C_{p,gas} |
198.29 | J/mol×K | 582.59 | Joback Calculated Property |

C_{p,gas} |
203.94 | J/mol×K | 609.53 | Joback Calculated Property |

C_{p,gas} |
209.35 | J/mol×K | 636.47 | Joback Calculated Property |

η | [0.0001265; 0.6060212] | Pa×s | [241.48; 474.84] | |

η | 0.6060212 | Pa×s | 241.48 | Joback Calculated Property |

η | 0.0554139 | Pa×s | 280.37 | Joback Calculated Property |

η | 0.0090753 | Pa×s | 319.27 | Joback Calculated Property |

η | 0.0022017 | Pa×s | 358.16 | Joback Calculated Property |

η | 0.0007050 | Pa×s | 397.05 | Joback Calculated Property |

η | 0.0002766 | Pa×s | 435.95 | Joback Calculated Property |

η | 0.0001265 | Pa×s | 474.84 | Joback Calculated Property |

P_{vap} |
[2.04e-03; 0.26] | kPa | [297.30; 357.50] | |

P_{vap} |
2.04e-03 ± 6.12e-05 | kPa | 297.30 | Vapor P... |

P_{vap} |
2.85e-03 ± 8.55e-05 | kPa | 300.40 | Vapor P... |

P_{vap} |
3.64e-03 ± 1.09e-04 | kPa | 303.40 | Vapor P... |

P_{vap} |
4.90e-03 ± 1.47e-04 | kPa | 306.40 | Vapor P... |

P_{vap} |
6.61e-03 ± 1.98e-04 | kPa | 309.40 | Vapor P... |

P_{vap} |
8.41e-03 ± 2.52e-04 | kPa | 312.40 | Vapor P... |

P_{vap} |
8.61e-03 ± 2.58e-04 | kPa | 312.50 | Vapor P... |

P_{vap} |
9.96e-03 ± 2.99e-04 | kPa | 314.50 | Vapor P... |

P_{vap} |
0.01 ± 0.00 | kPa | 316.40 | Vapor P... |

P_{vap} |
0.01 ± 0.00 | kPa | 318.50 | Vapor P... |

P_{vap} |
0.02 ± 0.00 | kPa | 319.50 | Vapor P... |

P_{vap} |
0.02 ± 0.00 | kPa | 321.40 | Vapor P... |

P_{vap} |
0.02 ± 0.00 | kPa | 322.50 | Vapor P... |

P_{vap} |
0.02 ± 0.00 | kPa | 323.50 | Vapor P... |

P_{vap} |
0.02 ± 0.00 | kPa | 323.60 | Vapor P... |

P_{vap} |
0.03 ± 0.00 | kPa | 326.40 | Vapor P... |

P_{vap} |
0.03 ± 0.00 | kPa | 326.60 | Vapor P... |

P_{vap} |
0.03 ± 0.00 | kPa | 328.50 | Vapor P... |

P_{vap} |
0.03 ± 0.00 | kPa | 328.60 | Vapor P... |

P_{vap} |
0.04 ± 0.00 | kPa | 331.40 | Vapor P... |

P_{vap} |
0.05 ± 0.00 | kPa | 333.40 | Vapor P... |

P_{vap} |
0.06 ± 0.00 | kPa | 336.30 | Vapor P... |

P_{vap} |
0.07 ± 0.00 | kPa | 338.60 | Vapor P... |

P_{vap} |
0.09 ± 0.00 | kPa | 341.40 | Vapor P... |

P_{vap} |
0.09 ± 0.00 | kPa | 342.60 | Vapor P... |

P_{vap} |
0.11 ± 0.00 | kPa | 343.50 | Vapor P... |

P_{vap} |
0.14 ± 0.00 | kPa | 347.60 | Vapor P... |

P_{vap} |
0.16 ± 0.00 | kPa | 349.30 | Vapor P... |

P_{vap} |
0.19 ± 0.01 | kPa | 352.50 | Vapor P... |

P_{vap} |
0.24 ± 0.01 | kPa | 355.40 | Vapor P... |

P_{vap} |
0.26 ± 0.01 | kPa | 357.50 | Vapor P... |

Find more compounds similar to *Propane-1,3-diol, 2-methyl-*.

- Crippen Method
- Crippen Method
- Vapor Pressures and Enthalpies of Vaporization of a Series of the 1,3-Alkanediols
- Joback Method
- McGowan Method
- NIST Webbook

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