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

Δ_{c}H°_{solid} |
-6227.00 | kJ/mol | NIST |

Δ_{f}G° |
-426.10 | kJ/mol | Joback Calculated Property |

Δ_{f}H°_{gas} |
-759.97 | kJ/mol | Joback Calculated Property |

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

Δ_{vap}H° |
82.30 ± 0.40 | kJ/mol | NIST |

log_{10}WS |
-2.15 | Crippen Calculated Property | |

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

McVol | 180.730 | ml/mol | McGowan Calculated Property |

P_{c} |
2100.34 | kPa | Joback Calculated Property |

I_{np} |
[263.80; 1550.00] | ||

I_{np} |
1511.00 | NIST | |

I_{np} |
1512.00 | NIST | |

I_{np} |
1511.00 | NIST | |

I_{np} |
1511.00 | NIST | |

I_{np} |
1510.00 | NIST | |

I_{np} |
1485.00 | NIST | |

I_{np} |
1548.00 | NIST | |

I_{np} |
1519.00 | NIST | |

I_{np} |
1548.10 | NIST | |

I_{np} |
1548.00 | NIST | |

I_{np} |
1550.00 | NIST | |

I_{np} |
1510.00 | NIST | |

I_{np} |
1513.00 | NIST | |

I_{np} |
1519.00 | NIST | |

I_{np} |
Outlier 266.60 | NIST | |

I_{np} |
Outlier 263.80 | NIST | |

I_{np} |
Outlier 266.60 | NIST | |

I_{np} |
1548.10 | NIST | |

I_{np} |
1513.00 | NIST | |

I_{np} |
1548.00 | NIST | |

I_{np} |
1512.00 | NIST | |

I | [2101.00; 2101.00] | ||

I | 2101.00 | NIST | |

I | 2101.00 | NIST | |

I | 2101.00 | NIST | |

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

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

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

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

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

C_{p,gas} |
[465.03; 539.69] | J/mol×K | [603.66; 782.25] | |

C_{p,gas} |
465.03 | J/mol×K | 603.66 | Joback Calculated Property |

C_{p,gas} |
478.94 | J/mol×K | 633.43 | Joback Calculated Property |

C_{p,gas} |
492.26 | J/mol×K | 663.19 | Joback Calculated Property |

C_{p,gas} |
505.00 | J/mol×K | 692.96 | Joback Calculated Property |

C_{p,gas} |
517.15 | J/mol×K | 722.72 | Joback Calculated Property |

C_{p,gas} |
528.71 | J/mol×K | 752.49 | Joback Calculated Property |

C_{p,gas} |
539.69 | J/mol×K | 782.25 | Joback Calculated Property |

η | [0.0001703; 0.0018153] | Pa×s | [358.05; 603.66] | |

η | 0.0018153 | Pa×s | 358.05 | Joback Calculated Property |

η | 0.0009995 | Pa×s | 398.99 | Joback Calculated Property |

η | 0.0006149 | Pa×s | 439.92 | Joback Calculated Property |

η | 0.0004109 | Pa×s | 480.86 | Joback Calculated Property |

η | 0.0002926 | Pa×s | 521.79 | Joback Calculated Property |

η | 0.0002188 | Pa×s | 562.73 | Joback Calculated Property |

η | 0.0001703 | Pa×s | 603.66 | Joback Calculated Property |

Δ_{vap}H |
63.60 | kJ/mol | 476.50 | NIST |

P_{vap} |
[1.90e-04; 0.11] | kPa | [298.10; 373.80] | |

P_{vap} |
1.90e-04 | kPa | 298.10 | Vapor P... |

P_{vap} |
2.80e-04 | kPa | 303.10 | Vapor P... |

P_{vap} |
5.40e-04 | kPa | 308.10 | Vapor P... |

P_{vap} |
8.00e-04 | kPa | 313.20 | Vapor P... |

P_{vap} |
8.40e-04 | kPa | 313.20 | Vapor P... |

P_{vap} |
1.38e-03 | kPa | 318.20 | Vapor P... |

P_{vap} |
1.31e-03 | kPa | 318.20 | Vapor P... |

P_{vap} |
1.67e-03 | kPa | 320.20 | Vapor P... |

P_{vap} |
1.64e-03 | kPa | 320.20 | Vapor P... |

P_{vap} |
2.26e-03 | kPa | 323.30 | Vapor P... |

P_{vap} |
2.28e-03 | kPa | 323.40 | Vapor P... |

P_{vap} |
2.78e-03 | kPa | 325.30 | Vapor P... |

P_{vap} |
3.35e-03 | kPa | 328.30 | Vapor P... |

P_{vap} |
3.62e-03 | kPa | 328.30 | Vapor P... |

P_{vap} |
4.66e-03 | kPa | 330.80 | Vapor P... |

P_{vap} |
5.49e-03 | kPa | 333.40 | Vapor P... |

P_{vap} |
5.61e-03 | kPa | 333.40 | Vapor P... |

P_{vap} |
7.11e-03 | kPa | 335.90 | Vapor P... |

P_{vap} |
7.71e-03 | kPa | 338.40 | Vapor P... |

P_{vap} |
8.58e-03 | kPa | 338.40 | Vapor P... |

P_{vap} |
0.01 | kPa | 341.00 | Vapor P... |

P_{vap} |
0.01 | kPa | 343.40 | Vapor P... |

P_{vap} |
0.01 | kPa | 343.80 | Vapor P... |

P_{vap} |
0.02 | kPa | 348.50 | Vapor P... |

P_{vap} |
0.02 | kPa | 348.60 | Vapor P... |

P_{vap} |
0.02 | kPa | 351.10 | Vapor P... |

P_{vap} |
0.03 | kPa | 353.60 | Vapor P... |

P_{vap} |
0.02 | kPa | 353.60 | Vapor P... |

P_{vap} |
0.03 | kPa | 353.60 | Vapor P... |

P_{vap} |
0.04 | kPa | 358.60 | Vapor P... |

P_{vap} |
0.04 | kPa | 358.70 | Vapor P... |

P_{vap} |
0.04 | kPa | 360.20 | Vapor P... |

P_{vap} |
0.05 | kPa | 363.70 | Vapor P... |

P_{vap} |
0.05 | kPa | 363.70 | Vapor P... |

P_{vap} |
0.07 | kPa | 366.20 | Vapor P... |

P_{vap} |
0.08 | kPa | 368.90 | Vapor P... |

P_{vap} |
0.08 | kPa | 368.90 | Vapor P... |

P_{vap} |
0.09 | kPa | 371.30 | Vapor P... |

P_{vap} |
0.09 | kPa | 371.30 | Vapor P... |

P_{vap} |
0.11 | kPa | 373.80 | Vapor P... |

P_{vap} |
0.10 | kPa | 373.80 | Vapor P... |

Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|

T_{boilr} |
429.20 | K | 2.70 | NIST |

Find more compounds similar to *Nonanedioic acid, dimethyl ester*.

- Crippen Method
- Crippen Method
- Vapor Pressures, Enthalpies of Vaporization, and Critical Parameters of a Series of Linear Aliphatic Dimethyl Esters of Dicarboxylic Acids
- Joback Method
- McGowan Method
- NIST Webbook

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that the value is more than 2 standard deviations away from the
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