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

Δ_{f}G° |
-49.16 | kJ/mol | Joback Calculated Property |

Δ_{f}H°_{gas} |
-440.73 | kJ/mol | Joback Calculated Property |

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

Δ_{vap}H° |
42.12 | kJ/mol | Joback Calculated Property |

log_{10}WS |
-3.80 | Crippen Calculated Property | |

logP_{oct/wat} |
4.018 | Crippen Calculated Property | |

McVol | 185.810 | ml/mol | McGowan Calculated Property |

P_{c} |
1812.32 | kPa | Joback Calculated Property |

I_{np} |
1116.00 | NIST | |

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

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

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

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

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

C_{p,gas} |
[440.40; 540.65] | J/mol×K | [489.92; 669.76] | |

C_{p,gas} |
440.40 | J/mol×K | 489.92 | Joback Calculated Property |

C_{p,gas} |
459.32 | J/mol×K | 519.89 | Joback Calculated Property |

C_{p,gas} |
477.30 | J/mol×K | 549.87 | Joback Calculated Property |

C_{p,gas} |
494.39 | J/mol×K | 579.84 | Joback Calculated Property |

C_{p,gas} |
510.62 | J/mol×K | 609.81 | Joback Calculated Property |

C_{p,gas} |
526.03 | J/mol×K | 639.79 | Joback Calculated Property |

C_{p,gas} |
540.65 | J/mol×K | 669.76 | Joback Calculated Property |

η | [0.0001691; 0.0086566] | Pa×s | [252.07; 489.92] | |

η | 0.0086566 | Pa×s | 252.07 | Joback Calculated Property |

η | 0.0028767 | Pa×s | 291.71 | Joback Calculated Property |

η | 0.0012443 | Pa×s | 331.35 | Joback Calculated Property |

η | 0.0006438 | Pa×s | 371.00 | Joback Calculated Property |

η | 0.0003783 | Pa×s | 410.64 | Joback Calculated Property |

η | 0.0002441 | Pa×s | 450.28 | Joback Calculated Property |

η | 0.0001691 | Pa×s | 489.92 | Joback Calculated Property |

P_{vap} |
[0.01; 0.17] | kPa | [278.30; 314.20] | |

P_{vap} |
0.01 | kPa | 278.30 | Determi... |

P_{vap} |
0.02 | kPa | 281.30 | Determi... |

P_{vap} |
0.02 | kPa | 284.30 | Determi... |

P_{vap} |
0.03 | kPa | 287.30 | Determi... |

P_{vap} |
0.03 | kPa | 290.30 | Determi... |

P_{vap} |
0.04 | kPa | 293.30 | Determi... |

P_{vap} |
0.05 | kPa | 296.30 | Determi... |

P_{vap} |
0.07 | kPa | 299.20 | Determi... |

P_{vap} |
0.08 | kPa | 302.20 | Determi... |

P_{vap} |
0.10 | kPa | 305.20 | Determi... |

P_{vap} |
0.12 | kPa | 308.20 | Determi... |

P_{vap} |
0.15 | kPa | 311.20 | Determi... |

P_{vap} |
0.17 | kPa | 314.20 | Determi... |

Find more compounds similar to *Butyl tert-octyl ether*.

- Crippen Method
- Crippen Method
- Determination of Ambient Temperature Vapor Pressures and Vaporization Enthalpies of Branched Ethers
- Joback Method
- McGowan Method
- NIST Webbook

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