- InChI
- InChI=1S/C19H40/c1-3-5-7-9-11-13-15-17-19-18-16-14-12-10-8-6-4-2/h3-19H2,1-2H3
- InChI Key
- LQERIDTXQFOHKA-UHFFFAOYSA-N
- Formula
- C19H40
- SMILES
- CCCCCCCCCCCCCCCCCCC
- Molecular Weight1
- 268.52
- CAS
- 629-92-5
- Other Names
-
- n-Nonadecane
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- vspec : Specific Volume (m3/kg).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.8270 | KDB | |
| ΔcH°liquid | -12662.60 ± 2.60 | kJ/mol | NIST |
| ΔfG° | 109.00 | kJ/mol | KDB |
| ΔfH°gas | [-435.40; -435.10] | kJ/mol |
|
| ΔfH°gas | -435.40 | kJ/mol | KDB |
| ΔfH°gas | -435.10 ± 2.90 | kJ/mol | NIST |
| ΔfH°liquid | -530.90 ± 2.90 | kJ/mol | NIST |
| ΔfusH° | 44.97 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 143.60 | kJ/mol | NIST |
| ΔvapH° | [95.80; 96.40] | kJ/mol |
|
| ΔvapH° | 96.40 | kJ/mol | NIST |
| ΔvapH° | 95.80 | kJ/mol | NIST |
| log10WS | -7.78 | Crippen Calculated Property | |
| logPoct/wat | 7.658 | Crippen Calculated Property | |
| McVol | 278.570 | ml/mol | McGowan Calculated Property |
| Pc | [1160.00; 1200.00] | kPa |
|
| Pc | 1160.00 | kPa | KDB |
| Pc | 1200.00 ± 200.00 | kPa | NIST |
| Pc | 1160.00 ± 40.00 | kPa | NIST |
| Tboil | [601.70; 603.00] | K |
|
| Tboil | 603.00 | K | KDB |
| Tboil | 602.90 | K | NIST |
| Tboil | 601.70 ± 1.50 | K | NIST |
| Tc | [755.00; 757.00] | K |
|
| Tc | 755.00 | K | KDB |
| Tc | 757.00 | K | Critica... |
| Tc | 755.00 ± 8.00 | K | NIST |
| Tc | 755.30 ± 3.00 | K | NIST |
| Tfus | [300.30; 305.80] | K |
|
| Tfus | 305.20 | K | KDB |
| Tfus | 304.35 ± 0.50 | K | NIST |
| Tfus | 304.00 ± 0.10 | K | NIST |
| Tfus | 303.95 ± 0.10 | K | NIST |
| Tfus | 305.20 ± 0.30 | K | NIST |
| Tfus | 305.80 ± 0.50 | K | NIST |
| Tfus | 304.90 ± 0.20 | K | NIST |
| Tfus | 304.60 ± 0.50 | K | NIST |
| Tfus | Outlier 300.30 ± 3.00 | K | NIST |
| Tfus | 305.00 ± 4.00 | K | NIST |
| Tfus | 305.00 ± 3.00 | K | NIST |
| Ttriple | 295.50 | K | Solubil... |
| Vc | 1.130 | m3/kmol | KDB |
| Zc | 0.2088110 | KDB | |
| Zra | 0.22 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [781.39; 892.50] | J/mol×K | [634.12; 793.53] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 780 800 820 840 860 880 900 650 700 750 | ||||
| Cp,gas | 781.39 | J/mol×K | 634.12 | Joback Calculated Property |
| Cp,gas | 801.89 | J/mol×K | 660.69 | Joback Calculated Property |
| Cp,gas | 821.56 | J/mol×K | 687.26 | Joback Calculated Property |
| Cp,gas | 840.44 | J/mol×K | 713.82 | Joback Calculated Property |
| Cp,gas | 858.54 | J/mol×K | 740.39 | Joback Calculated Property |
| Cp,gas | 875.88 | J/mol×K | 766.96 | Joback Calculated Property |
| Cp,gas | 892.50 | J/mol×K | 793.53 | Joback Calculated Property |
| Cp,liquid | [602.60; 640.00] | J/mol×K | [313.15; 353.00] |
|
| Cp,liquid | 602.60 | J/mol×K | 313.15 | NIST |
| Cp,liquid | 640.00 | J/mol×K | 353.00 | NIST |
| η | [0.0001095; 0.0040004] | Pa×s | [303.89; 634.12] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 300 400 500 600 | ||||
| η | 0.0040004 | Pa×s | 303.89 | Joback Calculated Property |
| η | 0.0013868 | Pa×s | 358.93 | Joback Calculated Property |
| η | 0.0006372 | Pa×s | 413.97 | Joback Calculated Property |
| η | 0.0003514 | Pa×s | 469.00 | Joback Calculated Property |
| η | 0.0002196 | Pa×s | 524.04 | Joback Calculated Property |
| η | 0.0001501 | Pa×s | 579.08 | Joback Calculated Property |
| η | 0.0001095 | Pa×s | 634.12 | Joback Calculated Property |
| ΔfusH | [13.67; 47.40] | kJ/mol | [296.00; 305.30] |
|
| ΔfusH | 13.67 | kJ/mol | 296.00 | NIST |
| ΔfusH | 47.40 | kJ/mol | 304.00 | NIST |
| ΔfusH | 42.70 | kJ/mol | 304.40 | NIST |
| ΔfusH | 47.40 | kJ/mol | 305.30 | NIST |
| ΔsubH | 136.60 | kJ/mol | 295.50 | NIST |
| ΔvapH | [56.02; 76.20] | kJ/mol | [505.50; 603.20] |
|
| ΔvapH | 76.20 | kJ/mol | 505.50 | NIST |
| ΔvapH | 73.00 | kJ/mol | 531.00 | NIST |
| ΔvapH | 56.02 | kJ/mol | 603.20 | KDB |
| ρl | 789.00 | kg/m3 | 305.00 | KDB |
| ΔfusS | [46.20; 155.90] | J/mol×K | [296.00; 304.00] |
|
| ΔfusS | 46.20 | J/mol×K | 296.00 | NIST |
| ΔfusS | 155.90 | J/mol×K | 304.00 | NIST |
| γ | 0.03 | N/m | 323.20 | KDB |
| vspec | [0.00; 0.00] | m3/kg | [305.45; 576.05] |
|
|
T(K) Specific Volume (m3/kg) 1.30e-3 1.40e-3 1.50e-3 1.60e-3 1.70e-3 300 400 500 | ||||
| vspec | 0.00 | m3/kg | 305.45 | A simpl... |
| vspec | 0.00 | m3/kg | 307.55 | A simpl... |
| vspec | 0.00 | m3/kg | 309.55 | A simpl... |
| vspec | 0.00 | m3/kg | 311.65 | A simpl... |
| vspec | 0.00 | m3/kg | 313.65 | A simpl... |
| vspec | 0.00 | m3/kg | 315.75 | A simpl... |
| vspec | 0.00 | m3/kg | 317.75 | A simpl... |
| vspec | 0.00 | m3/kg | 319.85 | A simpl... |
| vspec | 0.00 | m3/kg | 321.95 | A simpl... |
| vspec | 0.00 | m3/kg | 323.95 | A simpl... |
| vspec | 0.00 | m3/kg | 326.05 | A simpl... |
| vspec | 0.00 | m3/kg | 328.05 | A simpl... |
| vspec | 0.00 | m3/kg | 330.15 | A simpl... |
| vspec | 0.00 | m3/kg | 332.25 | A simpl... |
| vspec | 0.00 | m3/kg | 334.25 | A simpl... |
| vspec | 0.00 | m3/kg | 336.35 | A simpl... |
| vspec | 0.00 | m3/kg | 338.35 | A simpl... |
| vspec | 0.00 | m3/kg | 340.45 | A simpl... |
| vspec | 0.00 | m3/kg | 342.55 | A simpl... |
| vspec | 0.00 | m3/kg | 344.55 | A simpl... |
| vspec | 0.00 | m3/kg | 346.65 | A simpl... |
| vspec | 0.00 | m3/kg | 348.65 | A simpl... |
| vspec | 0.00 | m3/kg | 350.75 | A simpl... |
| vspec | 0.00 | m3/kg | 352.85 | A simpl... |
| vspec | 0.00 | m3/kg | 354.85 | A simpl... |
| vspec | 0.00 | m3/kg | 356.95 | A simpl... |
| vspec | 0.00 | m3/kg | 358.95 | A simpl... |
| vspec | 0.00 | m3/kg | 361.05 | A simpl... |
| vspec | 0.00 | m3/kg | 363.15 | A simpl... |
| vspec | 0.00 | m3/kg | 365.15 | A simpl... |
| vspec | 0.00 | m3/kg | 367.25 | A simpl... |
| vspec | 0.00 | m3/kg | 369.25 | A simpl... |
| vspec | 0.00 | m3/kg | 371.35 | A simpl... |
| vspec | 0.00 | m3/kg | 373.45 | A simpl... |
| vspec | 0.00 | m3/kg | 375.45 | A simpl... |
| vspec | 0.00 | m3/kg | 377.55 | A simpl... |
| vspec | 0.00 | m3/kg | 379.55 | A simpl... |
| vspec | 0.00 | m3/kg | 381.65 | A simpl... |
| vspec | 0.00 | m3/kg | 383.75 | A simpl... |
| vspec | 0.00 | m3/kg | 385.75 | A simpl... |
| vspec | 0.00 | m3/kg | 387.85 | A simpl... |
| vspec | 0.00 | m3/kg | 389.85 | A simpl... |
| vspec | 0.00 | m3/kg | 391.95 | A simpl... |
| vspec | 0.00 | m3/kg | 393.95 | A simpl... |
| vspec | 0.00 | m3/kg | 396.05 | A simpl... |
| vspec | 0.00 | m3/kg | 398.15 | A simpl... |
| vspec | 0.00 | m3/kg | 400.15 | A simpl... |
| vspec | 0.00 | m3/kg | 402.25 | A simpl... |
| vspec | 0.00 | m3/kg | 404.25 | A simpl... |
| vspec | 0.00 | m3/kg | 406.35 | A simpl... |
| vspec | 0.00 | m3/kg | 408.45 | A simpl... |
| vspec | 0.00 | m3/kg | 410.45 | A simpl... |
| vspec | 0.00 | m3/kg | 412.55 | A simpl... |
| vspec | 0.00 | m3/kg | 414.55 | A simpl... |
| vspec | 0.00 | m3/kg | 416.65 | A simpl... |
| vspec | 0.00 | m3/kg | 418.75 | A simpl... |
| vspec | 0.00 | m3/kg | 420.75 | A simpl... |
| vspec | 0.00 | m3/kg | 422.85 | A simpl... |
| vspec | 0.00 | m3/kg | 424.85 | A simpl... |
| vspec | 0.00 | m3/kg | 426.95 | A simpl... |
| vspec | 0.00 | m3/kg | 429.05 | A simpl... |
| vspec | 0.00 | m3/kg | 431.05 | A simpl... |
| vspec | 0.00 | m3/kg | 433.15 | A simpl... |
| vspec | 0.00 | m3/kg | 435.15 | A simpl... |
| vspec | 0.00 | m3/kg | 437.25 | A simpl... |
| vspec | 0.00 | m3/kg | 439.35 | A simpl... |
| vspec | 0.00 | m3/kg | 441.35 | A simpl... |
| vspec | 0.00 | m3/kg | 443.45 | A simpl... |
| vspec | 0.00 | m3/kg | 445.45 | A simpl... |
| vspec | 0.00 | m3/kg | 447.55 | A simpl... |
| vspec | 0.00 | m3/kg | 449.65 | A simpl... |
| vspec | 0.00 | m3/kg | 451.65 | A simpl... |
| vspec | 0.00 | m3/kg | 453.75 | A simpl... |
| vspec | 0.00 | m3/kg | 455.75 | A simpl... |
| vspec | 0.00 | m3/kg | 457.85 | A simpl... |
| vspec | 0.00 | m3/kg | 459.95 | A simpl... |
| vspec | 0.00 | m3/kg | 461.95 | A simpl... |
| vspec | 0.00 | m3/kg | 464.05 | A simpl... |
| vspec | 0.00 | m3/kg | 466.05 | A simpl... |
| vspec | 0.00 | m3/kg | 468.15 | A simpl... |
| vspec | 0.00 | m3/kg | 470.25 | A simpl... |
| vspec | 0.00 | m3/kg | 472.25 | A simpl... |
| vspec | 0.00 | m3/kg | 474.35 | A simpl... |
| vspec | 0.00 | m3/kg | 476.35 | A simpl... |
| vspec | 0.00 | m3/kg | 478.45 | A simpl... |
| vspec | 0.00 | m3/kg | 480.45 | A simpl... |
| vspec | 0.00 | m3/kg | 482.55 | A simpl... |
| vspec | 0.00 | m3/kg | 484.65 | A simpl... |
| vspec | 0.00 | m3/kg | 486.65 | A simpl... |
| vspec | 0.00 | m3/kg | 488.75 | A simpl... |
| vspec | 0.00 | m3/kg | 490.75 | A simpl... |
| vspec | 0.00 | m3/kg | 492.85 | A simpl... |
| vspec | 0.00 | m3/kg | 494.95 | A simpl... |
| vspec | 0.00 | m3/kg | 496.95 | A simpl... |
| vspec | 0.00 | m3/kg | 499.05 | A simpl... |
| vspec | 0.00 | m3/kg | 501.05 | A simpl... |
| vspec | 0.00 | m3/kg | 503.15 | A simpl... |
| vspec | 0.00 | m3/kg | 505.25 | A simpl... |
| vspec | 0.00 | m3/kg | 507.25 | A simpl... |
| vspec | 0.00 | m3/kg | 509.35 | A simpl... |
| vspec | 0.00 | m3/kg | 511.35 | A simpl... |
| vspec | 0.00 | m3/kg | 513.45 | A simpl... |
| vspec | 0.00 | m3/kg | 515.55 | A simpl... |
| vspec | 0.00 | m3/kg | 517.55 | A simpl... |
| vspec | 0.00 | m3/kg | 519.65 | A simpl... |
| vspec | 0.00 | m3/kg | 521.65 | A simpl... |
| vspec | 0.00 | m3/kg | 523.75 | A simpl... |
| vspec | 0.00 | m3/kg | 525.85 | A simpl... |
| vspec | 0.00 | m3/kg | 531.35 | A simpl... |
| vspec | 0.00 | m3/kg | 533.25 | A simpl... |
| vspec | 0.00 | m3/kg | 535.25 | A simpl... |
| vspec | 0.00 | m3/kg | 537.15 | A simpl... |
| vspec | 0.00 | m3/kg | 539.15 | A simpl... |
| vspec | 0.00 | m3/kg | 541.05 | A simpl... |
| vspec | 0.00 | m3/kg | 543.05 | A simpl... |
| vspec | 0.00 | m3/kg | 544.95 | A simpl... |
| vspec | 0.00 | m3/kg | 546.85 | A simpl... |
| vspec | 0.00 | m3/kg | 548.85 | A simpl... |
| vspec | 0.00 | m3/kg | 550.75 | A simpl... |
| vspec | 0.00 | m3/kg | 552.75 | A simpl... |
| vspec | 0.00 | m3/kg | 554.65 | A simpl... |
| vspec | 0.00 | m3/kg | 556.65 | A simpl... |
| vspec | 0.00 | m3/kg | 558.55 | A simpl... |
| vspec | 0.00 | m3/kg | 560.45 | A simpl... |
| vspec | 0.00 | m3/kg | 562.45 | A simpl... |
| vspec | 0.00 | m3/kg | 564.35 | A simpl... |
| vspec | 0.00 | m3/kg | 566.35 | A simpl... |
| vspec | 0.00 | m3/kg | 568.25 | A simpl... |
| vspec | 0.00 | m3/kg | 570.25 | A simpl... |
| vspec | 0.00 | m3/kg | 572.15 | A simpl... |
| vspec | 0.00 | m3/kg | 574.05 | A simpl... |
| vspec | 0.00 | m3/kg | 576.05 | A simpl... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [455.49; 639.03] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47703e+01 | |||
| Coefficient B | -5.00471e+03 | |||
| Coefficient C | -1.09923e+02 | |||
| Temperature range, min. | 455.49 | |||
| Temperature range, max. | 639.03 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 | ||||
| Pvap | 1.33 | kPa | 455.49 | Calculated Property |
| Pvap | 2.99 | kPa | 475.88 | Calculated Property |
| Pvap | 6.15 | kPa | 496.28 | Calculated Property |
| Pvap | 11.78 | kPa | 516.67 | Calculated Property |
| Pvap | 21.19 | kPa | 537.06 | Calculated Property |
| Pvap | 36.14 | kPa | 557.46 | Calculated Property |
| Pvap | 58.84 | kPa | 577.85 | Calculated Property |
| Pvap | 91.97 | kPa | 598.24 | Calculated Property |
| Pvap | 138.71 | kPa | 618.64 | Calculated Property |
| Pvap | 202.66 | kPa | 639.03 | Calculated Property |
| Pvap | [1.97e-05; 1113.31] | kPa | [305.33; 755.93] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.75641e+02 | |||
| Coefficient B | -1.78211e+04 | |||
| Coefficient C | -2.25095e+01 | |||
| Coefficient D | 7.24611e-06 | |||
| Temperature range, min. | 305.33 | |||
| Temperature range, max. | 755.93 | |||
|
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 400 600 | ||||
| Pvap | 1.97e-05 | kPa | 305.33 | Calculated Property |
| Pvap | 3.05e-03 | kPa | 355.40 | Calculated Property |
| Pvap | 0.10 | kPa | 405.46 | Calculated Property |
| Pvap | 1.26 | kPa | 455.53 | Calculated Property |
| Pvap | 8.23 | kPa | 505.60 | Calculated Property |
| Pvap | 34.58 | kPa | 555.66 | Calculated Property |
| Pvap | 107.07 | kPa | 605.73 | Calculated Property |
| Pvap | 267.64 | kPa | 655.80 | Calculated Property |
| Pvap | 575.42 | kPa | 705.86 | Calculated Property |
| Pvap | 1113.31 | kPa | 755.93 | Calculated Property |
Similar Compounds
Find more compounds similar to Nonadecane.
Mixtures
- Di-n-propyl ether + Nonadecane
- n-Butyl ether + Nonadecane
- Butane, 1-chloro- + Nonadecane
- Octane, 1-chloro- + Nonadecane
- Carbon dioxide + Nonadecane
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Critical temperatures and pressures of C40, C44, and C60 normal alkanes measured by the pulse-heating technique
- A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
- Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
- Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.