- InChI
- InChI=1S/C12H26/c1-3-5-7-9-11-12-10-8-6-4-2/h3-12H2,1-2H3
- InChI Key
- SNRUBQQJIBEYMU-UHFFFAOYSA-N
- Formula
- C12H26
- SMILES
- CCCCCCCCCCCC
- Molecular Weight1
- 170.33
- CAS
- 112-40-3
- Other Names
-
- Adakane 12
- BIHEXYL
- Ba 51-090453
- CH3(CH2)10CH3
- Dihexyl
- Duodecane
- NSC 8714
- n-Dodecane
- 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).
- μ : Dipole Moment (debye).
- 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).
- NFPA Fire : NFPA Fire Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- D*i : Self diffusion coefficient (m2/s).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- αdiff : Thermal diffusivity (m2/s).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5750 | KDB | |
| ΔcH°liquid | [-8090.60; -7901.74] | kJ/mol |
|
| ΔcH°liquid | -7901.74 | kJ/mol | NIST |
| ΔcH°liquid | -8086.00 ± 1.20 | kJ/mol | NIST |
| ΔcH°liquid | -8083.20 | kJ/mol | NIST |
| ΔcH°liquid | -8090.60 ± 7.90 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| ΔfG° | 50.07 | kJ/mol | KDB |
| ΔfH°gas | [-291.10; -288.10] | kJ/mol |
|
| ΔfH°gas | -291.10 | kJ/mol | KDB |
| ΔfH°gas | -290.90 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -288.10 ± 3.30 | kJ/mol | NIST |
| ΔfH°liquid | [-352.10; -349.30] | kJ/mol |
|
| ΔfH°liquid | -352.10 ± 1.40 | kJ/mol | NIST |
| ΔfH°liquid | -349.30 ± 3.20 | kJ/mol | NIST |
| ΔfusH° | 26.84 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 100.20 | kJ/mol | NIST |
| ΔvapH° | 42.31 | kJ/mol | Joback Calculated Property |
| log10WS | -4.85 | Crippen Calculated Property | |
| logPoct/wat | 4.927 | Crippen Calculated Property | |
| McVol | 179.940 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| Pc | [1800.00; 1860.00] | kPa |
|
| Pc | 1820.00 | kPa | KDB |
| Pc | 1800.00 ± 100.00 | kPa | NIST |
| Pc | 1810.00 ± 20.00 | kPa | NIST |
| Pc | 1834.00 | kPa | NIST |
| Pc | 1860.00 ± 13.78 | kPa | NIST |
| Pc | 1824.00 ± 10.00 | kPa | NIST |
| ρc | [221.44; 226.55] | kg/m3 |
|
| ρc | 221.44 ± 17.03 | kg/m3 | NIST |
| ρc | 226.55 ± 6.81 | kg/m3 | NIST |
| Inp | [200.12; 209.90] |
|
|
| Inp | 200.12 | NIST | |
| Inp | 202.83 | NIST | |
| Inp | 209.90 | NIST | |
| S°gas | 622.50 | J/mol×K | NIST |
| S°liquid | [490.66; 497.10] | J/mol×K |
|
| S°liquid | 490.66 | J/mol×K | NIST |
| S°liquid | 497.10 | J/mol×K | NIST |
| Tboil | [479.15; 489.47] | K |
|
| Tboil | 489.47 | K | KDB |
| Tboil | 479.15 | K | Determi... |
| Tc | 658.00 | K | KDB |
| Tfus | [263.50; 264.95] | K |
|
| Tfus | 263.50 | K | KDB |
| Tfus | 263.70 | K | Determi... |
| Tfus | 264.95 | K | Density... |
| Vc | [0.754; 0.754] | m3/kmol |
|
| Vc | 0.754 | m3/kmol | KDB |
| Vc | 0.754 | m3/kmol | NIST |
| Zc | 0.2508300 | KDB | |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [406.83; 498.37] | J/mol×K | [473.96; 634.98] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 400 420 440 460 480 500 500 550 600 | ||||
| Cp,gas | 406.83 | J/mol×K | 473.96 | Joback Calculated Property |
| Cp,gas | 423.59 | J/mol×K | 500.80 | Joback Calculated Property |
| Cp,gas | 439.73 | J/mol×K | 527.63 | Joback Calculated Property |
| Cp,gas | 455.26 | J/mol×K | 554.47 | Joback Calculated Property |
| Cp,gas | 470.20 | J/mol×K | 581.30 | Joback Calculated Property |
| Cp,gas | 484.57 | J/mol×K | 608.14 | Joback Calculated Property |
| Cp,gas | 498.37 | J/mol×K | 634.98 | Joback Calculated Property |
| Cp,liquid | [368.47; 388.29] | J/mol×K | [283.15; 323.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 370 375 380 385 390 290 300 310 320 | ||||
| Cp,liquid | 368.47 | J/mol×K | 283.15 | Heat Ca... |
| Cp,liquid | 371.38 | J/mol×K | 288.15 | Thermod... |
| Cp,liquid | 370.48 | J/mol×K | 288.15 | Heat Ca... |
| Cp,liquid | 372.74 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 371.10 | J/mol×K | 297.70 | NIST |
| Cp,liquid | 374.50 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 375.26 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 370.72 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 374.82 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 375.93 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 375.94 | J/mol×K | 298.15 | Thermod... |
| Cp,liquid | 374.93 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 375.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 376.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 372.12 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 375.04 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 376.09 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 376.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 375.37 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 376.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 373.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 376.91 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 373.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 376.46 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 377.43 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 380.02 | J/mol×K | 308.15 | Heat Ca... |
| Cp,liquid | 380.92 | J/mol×K | 308.15 | Thermod... |
| Cp,liquid | 382.73 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 385.48 | J/mol×K | 318.15 | Heat Ca... |
| Cp,liquid | 386.31 | J/mol×K | 318.15 | Thermod... |
| Cp,liquid | 388.29 | J/mol×K | 323.15 | Heat Ca... |
| η | [0.0000551; 0.0015800] | Pa×s | [288.15; 673.20] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 300 400 500 600 | ||||
| η | 0.0015800 | Pa×s | 288.15 | Physica... |
| η | 0.0014540 | Pa×s | 293.15 | Dynamic... |
| η | 0.0014540 | Pa×s | 293.15 | Dynamic... |
| η | 0.0014700 | Pa×s | 293.15 | Physica... |
| η | 0.0013270 | Pa×s | 298.15 | Dynamic... |
| η | 0.0013500 | Pa×s | 298.15 | Physica... |
| η | 0.0013270 | Pa×s | 298.15 | Dynamic... |
| η | 0.0013360 | Pa×s | 298.15 | Densiti... |
| η | 0.0012190 | Pa×s | 303.15 | Dynamic... |
| η | 0.0012400 | Pa×s | 303.15 | Physica... |
| η | 0.0012190 | Pa×s | 303.15 | Dynamic... |
| η | 0.0012210 | Pa×s | 303.15 | Densiti... |
| η | 0.0013335 | Pa×s | 303.20 | Viscosi... |
| η | 0.0011400 | Pa×s | 308.15 | Physica... |
| η | 0.0011250 | Pa×s | 308.15 | Densiti... |
| η | 0.0010600 | Pa×s | 313.15 | Physica... |
| η | 0.0010390 | Pa×s | 313.15 | Densiti... |
| η | 0.0011221 | Pa×s | 313.20 | Viscosi... |
| η | 0.0009650 | Pa×s | 318.15 | Densiti... |
| η | 0.0009900 | Pa×s | 318.15 | Physica... |
| η | 0.0009700 | Pa×s | 323.00 | Viscosi... |
| η | 0.0008980 | Pa×s | 323.15 | Densiti... |
| η | 0.0009300 | Pa×s | 323.15 | Physica... |
| η | 0.0009225 | Pa×s | 323.15 | Liquid ... |
| η | 0.0008700 | Pa×s | 328.15 | Physica... |
| η | 0.0008430 | Pa×s | 328.15 | Densiti... |
| η | 0.0008519 | Pa×s | 333.10 | Viscosi... |
| η | 0.0008200 | Pa×s | 333.15 | Physica... |
| η | 0.0007442 | Pa×s | 343.30 | Viscosi... |
| η | 0.0006763 | Pa×s | 348.15 | Liquid ... |
| η | 0.0006736 | Pa×s | 353.30 | Viscosi... |
| η | 0.0006075 | Pa×s | 363.20 | Viscosi... |
| η | 0.0005070 | Pa×s | 373.15 | Liquid ... |
| η | 0.0005467 | Pa×s | 373.30 | Viscosi... |
| η | 0.0004902 | Pa×s | 383.20 | Viscosi... |
| η | 0.0004472 | Pa×s | 393.20 | Viscosi... |
| η | 0.0004003 | Pa×s | 398.15 | Liquid ... |
| η | 0.0004112 | Pa×s | 403.20 | Viscosi... |
| η | 0.0003785 | Pa×s | 413.20 | Viscosi... |
| η | 0.0003223 | Pa×s | 423.15 | Liquid ... |
| η | 0.0003508 | Pa×s | 423.20 | Viscosi... |
| η | 0.0003277 | Pa×s | 433.20 | Viscosi... |
| η | 0.0002974 | Pa×s | 443.40 | Viscosi... |
| η | 0.0002595 | Pa×s | 448.15 | Liquid ... |
| η | 0.0002822 | Pa×s | 453.10 | Viscosi... |
| η | 0.0002604 | Pa×s | 463.20 | Viscosi... |
| η | 0.0002156 | Pa×s | 473.15 | Liquid ... |
| η | 0.0002440 | Pa×s | 473.20 | Viscosi... |
| η | 0.0002250 | Pa×s | 483.10 | Viscosi... |
| η | 0.0002250 | Pa×s | 483.10 | Viscosi... |
| η | 0.0002076 | Pa×s | 493.20 | Viscosi... |
| η | 0.0001821 | Pa×s | 498.15 | Liquid ... |
| η | 0.0001964 | Pa×s | 503.20 | Viscosi... |
| η | 0.0001846 | Pa×s | 513.10 | Viscosi... |
| η | 0.0001532 | Pa×s | 523.15 | Liquid ... |
| η | 0.0001722 | Pa×s | 523.20 | Viscosi... |
| η | 0.0001608 | Pa×s | 533.10 | Viscosi... |
| η | 0.0001489 | Pa×s | 543.20 | Viscosi... |
| η | 0.0001277 | Pa×s | 548.15 | Liquid ... |
| η | 0.0001375 | Pa×s | 553.20 | Viscosi... |
| η | 0.0001297 | Pa×s | 563.20 | Viscosi... |
| η | 0.0001051 | Pa×s | 573.15 | Liquid ... |
| η | 0.0001201 | Pa×s | 573.20 | Viscosi... |
| η | 0.0001126 | Pa×s | 583.30 | Viscosi... |
| η | 0.0001031 | Pa×s | 593.20 | Viscosi... |
| η | 0.0000974 | Pa×s | 603.20 | Viscosi... |
| η | 0.0000913 | Pa×s | 613.20 | Viscosi... |
| η | 0.0000839 | Pa×s | 623.10 | Viscosi... |
| η | 0.0000767 | Pa×s | 633.20 | Viscosi... |
| η | 0.0000694 | Pa×s | 643.10 | Viscosi... |
| η | 0.0000657 | Pa×s | 653.20 | Viscosi... |
| η | 0.0000605 | Pa×s | 663.20 | Viscosi... |
| η | 0.0000551 | Pa×s | 673.20 | Viscosi... |
| η | 0.0000551 | Pa×s | 673.20 | Viscosi... |
| ΔfusH | [35.70; 36.84] | kJ/mol | [263.10; 263.60] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 35.6 35.8 36 36.2 36.4 36.6 36.8 263.2 263.4 263.6 | ||||
| ΔfusH | 35.70 | kJ/mol | 263.10 | NIST |
| ΔfusH | 36.58 | kJ/mol | 263.50 | NIST |
| ΔfusH | 36.84 | kJ/mol | 263.59 | NIST |
| ΔfusH | 36.82 | kJ/mol | 263.60 | NIST |
| ΔfusH | 36.82 | kJ/mol | 263.60 | NIST |
| ΔsubH | 101.70 | kJ/mol | 263.00 | NIST |
| ΔvapH | [43.64; 65.70] | kJ/mol | [299.00; 488.60] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 45 50 55 60 65 300 350 400 450 | ||||
| ΔvapH | 61.40 | kJ/mol | 299.00 | NIST |
| ΔvapH | 65.70 | kJ/mol | 317.00 | NIST |
| ΔvapH | 58.10 | kJ/mol | 334.00 | NIST |
| ΔvapH | 61.80 | kJ/mol | 339.00 | NIST |
| ΔvapH | 61.10 | kJ/mol | 343.50 | NIST |
| ΔvapH | 57.40 | kJ/mol | 344.00 | NIST |
| ΔvapH | 51.60 | kJ/mol | 446.00 | NIST |
| ΔvapH | 43.64 | kJ/mol | 488.60 | KDB |
| Pvap | [4.21e-03; 241.00] | kPa | [284.15; 509.15] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 400 500 | ||||
| Pvap | 4.21e-03 | kPa | 284.15 | Determi... |
| Pvap | 6.46e-03 | kPa | 289.15 | Determi... |
| Pvap | 9.78e-03 | kPa | 294.15 | Determi... |
| Pvap | 0.01 | kPa | 299.15 | Determi... |
| Pvap | 0.02 | kPa | 304.15 | Determi... |
| Pvap | 0.03 | kPa | 309.15 | Determi... |
| Pvap | 0.06 | kPa | 313.15 | Vapor-L... |
| Pvap | 0.06 | kPa | 313.15 | Vapor L... |
| Pvap | 0.04 | kPa | 314.15 | Determi... |
| Pvap | 0.06 | kPa | 319.15 | Determi... |
| Pvap | 0.20 | kPa | 323.15 | Isother... |
| Pvap | 0.09 | kPa | 324.15 | Determi... |
| Pvap | 0.12 | kPa | 329.15 | Determi... |
| Pvap | 0.17 | kPa | 334.15 | Determi... |
| Pvap | 0.23 | kPa | 339.15 | Determi... |
| Pvap | 0.36 | kPa | 342.18 | P-x dat... |
| Pvap | 0.40 | kPa | 343.15 | Bubble ... |
| Pvap | 0.32 | kPa | 344.15 | Determi... |
| Pvap | 0.42 | kPa | 349.15 | Determi... |
| Pvap | 0.75 | kPa | 352.68 | P-x dat... |
| Pvap | 0.70 | kPa | 353.15 | Bubble ... |
| Pvap | 0.56 | kPa | 354.15 | Determi... |
| Pvap | 0.75 | kPa | 359.15 | Determi... |
| Pvap | 1.20 | kPa | 363.15 | Bubble ... |
| Pvap | 0.98 | kPa | 364.15 | Determi... |
| Pvap | 1.27 | kPa | 369.15 | Determi... |
| Pvap | 2.00 | kPa | 373.15 | Bubble ... |
| Pvap | 1.64 | kPa | 374.15 | Determi... |
| Pvap | 2.10 | kPa | 379.15 | Determi... |
| Pvap | 3.20 | kPa | 383.15 | Bubble ... |
| Pvap | 2.67 | kPa | 384.15 | Determi... |
| Pvap | 3.38 | kPa | 389.15 | Determi... |
| Pvap | 4.90 | kPa | 393.15 | Bubble ... |
| Pvap | 4.25 | kPa | 394.15 | Determi... |
| Pvap | 5.32 | kPa | 399.15 | Determi... |
| Pvap | 6.62 | kPa | 404.15 | Determi... |
| Pvap | 8.19 | kPa | 409.15 | Determi... |
| Pvap | 10.10 | kPa | 414.15 | Determi... |
| Pvap | 12.40 | kPa | 419.15 | Determi... |
| Pvap | 15.10 | kPa | 424.15 | Determi... |
| Pvap | 18.30 | kPa | 429.15 | Determi... |
| Pvap | 20.90 | kPa | 432.23 | Isobari... |
| Pvap | 22.10 | kPa | 434.15 | Determi... |
| Pvap | 26.60 | kPa | 439.15 | Determi... |
| Pvap | 31.80 | kPa | 444.15 | Determi... |
| Pvap | 31.00 | kPa | 444.86 | Isobari... |
| Pvap | 38.00 | kPa | 449.15 | Determi... |
| Pvap | 40.00 | kPa | 453.92 | Low-Pre... |
| Pvap | 40.08 | kPa | 453.92 | Low-Pre... |
| Pvap | 45.10 | kPa | 454.15 | Determi... |
| Pvap | 42.70 | kPa | 455.87 | Isobari... |
| Pvap | 43.58 | kPa | 456.87 | Low-Pre... |
| Pvap | 53.40 | kPa | 459.15 | Determi... |
| Pvap | 46.71 | kPa | 459.31 | Low-Pre... |
| Pvap | 49.93 | kPa | 461.72 | Low-Pre... |
| Pvap | 50.80 | kPa | 462.05 | Isobari... |
| Pvap | 63.00 | kPa | 464.15 | Determi... |
| Pvap | 55.35 | kPa | 465.47 | Low-Pre... |
| Pvap | 58.41 | kPa | 467.52 | Low-Pre... |
| Pvap | 74.10 | kPa | 469.15 | Determi... |
| Pvap | 62.30 | kPa | 469.67 | Isobari... |
| Pvap | 63.63 | kPa | 470.69 | Low-Pre... |
| Pvap | 86.80 | kPa | 474.15 | Determi... |
| Pvap | 70.20 | kPa | 474.19 | Isobari... |
| Pvap | 69.97 | kPa | 474.33 | Low-Pre... |
| Pvap | 77.75 | kPa | 478.47 | Low-Pre... |
| Pvap | 101.00 | kPa | 479.15 | Determi... |
| Pvap | 81.00 | kPa | 479.82 | Isobari... |
| Pvap | 118.00 | kPa | 484.15 | Determi... |
| Pvap | 90.80 | kPa | 484.34 | Isobari... |
| Pvap | 100.60 | kPa | 488.50 | Isobari... |
| Pvap | 137.00 | kPa | 489.15 | Determi... |
| Pvap | 158.00 | kPa | 494.15 | Determi... |
| Pvap | 183.00 | kPa | 499.15 | Determi... |
| Pvap | 210.00 | kPa | 504.15 | Determi... |
| Pvap | 241.00 | kPa | 509.15 | Determi... |
| n0 | [1.40018; 1.42750] | [293.10; 343.15] |
|
|
|
T(K) Refractive Index 1.4 1.41 1.41 1.42 1.42 1.43 1.43 300 320 340 | ||||
| n0 | 1.42200 | 293.10 | Extract... | |
| n0 | 1.42200 | 293.10 | Phase e... | |
| n0 | 1.42210 | 293.10 | Extract... | |
| n0 | 1.42200 | 293.10 | Evaluat... | |
| n0 | 1.42200 | 293.10 | Liquid ... | |
| n0 | 1.41920 | 293.15 | Isother... | |
| n0 | 1.42155 | 293.15 | Liquid ... | |
| n0 | 1.42100 | 293.15 | Activit... | |
| n0 | 1.42180 | 293.15 | Experim... | |
| n0 | 1.42218 | 293.15 | Thermod... | |
| n0 | 1.42100 | 293.15 | Physica... | |
| n0 | 1.42180 | 293.15 | Vapor L... | |
| n0 | 1.41860 | 298.15 | Excess ... | |
| n0 | 1.41920 | 298.15 | Correla... | |
| n0 | 1.42011 | 298.15 | (Liquid... | |
| n0 | 1.42011 | 298.15 | Thiophe... | |
| n0 | 1.41960 | 298.15 | Liquid ... | |
| n0 | 1.41720 | 298.15 | Physica... | |
| n0 | 1.42750 | 298.15 | Liquid-... | |
| n0 | 1.42750 | 298.15 | Liquid-... | |
| n0 | 1.41970 | 298.15 | Measure... | |
| n0 | 1.41970 | 298.15 | Thermod... | |
| n0 | 1.41960 | 298.20 | Liquid-... | |
| n0 | 1.41640 | 303.15 | Excess ... | |
| n0 | 1.41810 | 303.15 | Liquid ... | |
| n0 | 1.41350 | 303.15 | Physica... | |
| n0 | 1.41784 | 303.15 | Thermod... | |
| n0 | 1.41400 | 308.15 | Excess ... | |
| n0 | 1.41346 | 313.15 | Thermod... | |
| n0 | 1.41310 | 313.20 | Liquid-... | |
| n0 | 1.40914 | 323.15 | Thermod... | |
| n0 | 1.40479 | 333.15 | Thermod... | |
| n0 | 1.40018 | 343.15 | Thermod... | |
| ρl | [610.60; 752.44] | kg/m3 | [288.15; 473.15] |
|
|
T(K) Liquid Density (kg/m3) 600 650 700 750 300 350 400 450 | ||||
| ρl | 752.35 | kg/m3 | 288.15 | Thermop... |
| ρl | 752.44 | kg/m3 | 288.15 | Permitt... |
| ρl | 752.41 | kg/m3 | 288.15 | Densiti... |
| ρl | 748.00 | kg/m3 | 293.00 | KDB |
| ρl | 748.73 | kg/m3 | 293.15 | Densiti... |
| ρl | 748.83 | kg/m3 | 293.15 | Densiti... |
| ρl | 748.72 | kg/m3 | 293.15 | Thermop... |
| ρl | 748.79 | kg/m3 | 293.15 | Density... |
| ρl | 748.83 | kg/m3 | 293.15 | Densiti... |
| ρl | 748.80 | kg/m3 | 293.15 | Permitt... |
| ρl | 748.79 | kg/m3 | 293.15 | Densiti... |
| ρl | 749.00 | kg/m3 | 293.15 | Excess ... |
| ρl | 748.81 | kg/m3 | 293.15 | Thermop... |
| ρl | 748.89 | kg/m3 | 293.15 | Density... |
| ρl | 745.38 | kg/m3 | 298.15 | Excess ... |
| ρl | 745.28 | kg/m3 | 298.15 | Excess ... |
| ρl | 745.38 | kg/m3 | 298.15 | Excess ... |
| ρl | 745.38 | kg/m3 | 298.15 | Excess ... |
| ρl | 745.52 | kg/m3 | 298.15 | Thermod... |
| ρl | 745.28 | kg/m3 | 298.15 | Excess ... |
| ρl | 745.27 | kg/m3 | 298.15 | Water/o... |
| ρl | 745.20 | kg/m3 | 298.15 | (Liquid... |
| ρl | 745.62 | kg/m3 | 298.15 | Thermod... |
| ρl | 745.32 | kg/m3 | 298.15 | Solvent... |
| ρl | 745.21 | kg/m3 | 298.15 | Binary ... |
| ρl | 745.82 | kg/m3 | 298.15 | Solid L... |
| ρl | 741.54 | kg/m3 | 298.15 | Thermod... |
| ρl | 741.54 | kg/m3 | 298.15 | Thermod... |
| ρl | 745.38 | kg/m3 | 298.15 | Excess ... |
| ρl | 745.41 | kg/m3 | 298.15 | Mutual ... |
| ρl | 745.32 | kg/m3 | 298.15 | Excess ... |
| ρl | 745.19 | kg/m3 | 298.15 | Permitt... |
| ρl | 745.52 | kg/m3 | 298.15 | Thermod... |
| ρl | 745.09 | kg/m3 | 298.15 | Thermop... |
| ρl | 745.28 | kg/m3 | 298.15 | Study o... |
| ρl | 745.51 | kg/m3 | 298.15 | Liquid ... |
| ρl | 745.22 | kg/m3 | 298.15 | Densiti... |
| ρl | 741.52 | kg/m3 | 298.15 | Liquid ... |
| ρl | 745.11 | kg/m3 | 298.15 | Densiti... |
| ρl | 745.28 | kg/m3 | 298.15 | Excess ... |
| ρl | 741.54 | kg/m3 | 298.15 | Liquid-... |
| ρl | 747.00 | kg/m3 | 298.15 | Ternary... |
| ρl | 745.52 | kg/m3 | 298.15 | Liquid-... |
| ρl | 745.23 | kg/m3 | 298.15 | Densiti... |
| ρl | 741.54 | kg/m3 | 298.15 | Thermod... |
| ρl | 745.51 | kg/m3 | 298.15 | Liquid-... |
| ρl | 745.16 | kg/m3 | 298.15 | Densiti... |
| ρl | 746.60 | kg/m3 | 298.20 | Ternary... |
| ρl | 745.15 | kg/m3 | 298.20 | Apparen... |
| ρl | 741.57 | kg/m3 | 303.15 | Permitt... |
| ρl | 741.77 | kg/m3 | 303.15 | Densiti... |
| ρl | 741.75 | kg/m3 | 303.15 | Excess ... |
| ρl | 741.53 | kg/m3 | 303.15 | Densiti... |
| ρl | 741.98 | kg/m3 | 303.15 | Thermod... |
| ρl | 741.42 | kg/m3 | 303.15 | Thermop... |
| ρl | 741.63 | kg/m3 | 303.15 | Density... |
| ρl | 741.54 | kg/m3 | 303.15 | Density... |
| ρl | 741.60 | kg/m3 | 303.15 | Densiti... |
| ρl | 741.59 | kg/m3 | 303.15 | Densiti... |
| ρl | 741.46 | kg/m3 | 303.15 | Thermop... |
| ρl | 737.97 | kg/m3 | 308.15 | Densiti... |
| ρl | 738.34 | kg/m3 | 308.15 | Thermod... |
| ρl | 737.93 | kg/m3 | 308.15 | Permitt... |
| ρl | 737.95 | kg/m3 | 308.15 | Densiti... |
| ρl | 738.12 | kg/m3 | 308.15 | Excess ... |
| ρl | 734.08 | kg/m3 | 313.15 | Thermop... |
| ρl | 734.33 | kg/m3 | 313.15 | Densiti... |
| ρl | 734.35 | kg/m3 | 313.15 | Density... |
| ρl | 734.25 | kg/m3 | 313.15 | Density... |
| ρl | 734.48 | kg/m3 | 313.15 | Excess ... |
| ρl | 734.87 | kg/m3 | 313.15 | Densiti... |
| ρl | 734.18 | kg/m3 | 313.15 | Thermop... |
| ρl | 734.25 | kg/m3 | 313.15 | Densiti... |
| ρl | 734.31 | kg/m3 | 313.15 | Densiti... |
| ρl | 734.19 | kg/m3 | 313.15 | Thermop... |
| ρl | 734.69 | kg/m3 | 313.15 | Thermod... |
| ρl | 734.33 | kg/m3 | 313.20 | Apparen... |
| ρl | 730.70 | kg/m3 | 318.15 | Permitt... |
| ρl | 730.68 | kg/m3 | 318.15 | Densiti... |
| ρl | 730.66 | kg/m3 | 318.15 | Densiti... |
| ρl | 731.03 | kg/m3 | 318.15 | Thermod... |
| ρl | 726.74 | kg/m3 | 323.15 | Thermop... |
| ρl | 727.01 | kg/m3 | 323.15 | Densiti... |
| ρl | 726.88 | kg/m3 | 323.15 | Densiti... |
| ρl | 726.94 | kg/m3 | 323.15 | Density... |
| ρl | 726.94 | kg/m3 | 323.15 | Densiti... |
| ρl | 727.37 | kg/m3 | 323.15 | Thermod... |
| ρl | 726.88 | kg/m3 | 323.15 | Thermop... |
| ρl | 727.00 | kg/m3 | 323.15 | Densiti... |
| ρl | 727.04 | kg/m3 | 323.15 | Density... |
| ρl | 723.33 | kg/m3 | 328.15 | Densiti... |
| ρl | 723.32 | kg/m3 | 328.15 | Permitt... |
| ρl | 723.35 | kg/m3 | 328.15 | Densiti... |
| ρl | 719.53 | kg/m3 | 333.15 | Thermop... |
| ρl | 719.69 | kg/m3 | 333.15 | Density... |
| ρl | 719.38 | kg/m3 | 333.15 | Thermop... |
| ρl | 719.59 | kg/m3 | 333.15 | Densiti... |
| ρl | 719.67 | kg/m3 | 333.15 | Densiti... |
| ρl | 719.59 | kg/m3 | 333.15 | Density... |
| ρl | 719.65 | kg/m3 | 333.15 | Densiti... |
| ρl | 719.53 | kg/m3 | 333.15 | Densiti... |
| ρl | 715.98 | kg/m3 | 338.15 | Densiti... |
| ρl | 712.20 | kg/m3 | 343.15 | Density... |
| ρl | 712.20 | kg/m3 | 343.15 | Density... |
| ρl | 712.28 | kg/m3 | 343.15 | Densiti... |
| ρl | 711.32 | kg/m3 | 343.15 | Thermop... |
| ρl | 712.10 | kg/m3 | 344.15 | High-pr... |
| ρl | 704.62 | kg/m3 | 353.15 | Thermop... |
| ρl | 704.70 | kg/m3 | 353.15 | Density... |
| ρl | 697.10 | kg/m3 | 363.15 | Density... |
| ρl | 697.21 | kg/m3 | 363.15 | Thermop... |
| ρl | 689.60 | kg/m3 | 373.15 | Density... |
| ρl | 689.75 | kg/m3 | 373.15 | Thermop... |
| ρl | 682.25 | kg/m3 | 383.15 | Thermop... |
| ρl | 674.68 | kg/m3 | 393.15 | Thermop... |
| ρl | 667.04 | kg/m3 | 403.15 | Thermop... |
| ρl | 659.32 | kg/m3 | 413.15 | Thermop... |
| ρl | 651.53 | kg/m3 | 423.15 | Thermop... |
| ρl | 643.60 | kg/m3 | 433.15 | Thermop... |
| ρl | 635.55 | kg/m3 | 443.15 | Thermop... |
| ρl | 627.38 | kg/m3 | 453.15 | Thermop... |
| ρl | 619.09 | kg/m3 | 463.15 | Thermop... |
| ρl | 610.60 | kg/m3 | 473.15 | Thermop... |
| D*i | [0.00; 0.00] | m2/s | [264.14; 364.54] |
|
|
T(K) Self diffusion coefficient (m2/s) 5.00e-10 1.00e-9 1.50e-9 2.00e-9 2.50e-9 300 350 | ||||
| D*i | 0.00 | m2/s | 264.14 | Viscous... |
| D*i | 0.00 | m2/s | 266.50 | Viscous... |
| D*i | 0.00 | m2/s | 268.03 | Viscous... |
| D*i | 0.00 | m2/s | 278.20 | Viscous... |
| D*i | 0.00 | m2/s | 278.52 | Viscous... |
| D*i | 0.00 | m2/s | 278.56 | Viscous... |
| D*i | 0.00 | m2/s | 278.72 | Viscous... |
| D*i | 0.00 | m2/s | 288.09 | Viscous... |
| D*i | 0.00 | m2/s | 288.49 | Viscous... |
| D*i | 0.00 | m2/s | 288.52 | Viscous... |
| D*i | 0.00 | m2/s | 298.15 | Viscous... |
| D*i | 0.00 | m2/s | 298.20 | Viscous... |
| D*i | 0.00 | m2/s | 298.21 | Viscous... |
| D*i | 0.00 | m2/s | 308.15 | Viscous... |
| D*i | 0.00 | m2/s | 308.16 | Viscous... |
| D*i | 0.00 | m2/s | 318.15 | Viscous... |
| D*i | 0.00 | m2/s | 318.16 | Viscous... |
| D*i | 0.00 | m2/s | 323.17 | Viscous... |
| D*i | 0.00 | m2/s | 328.17 | Viscous... |
| D*i | 0.00 | m2/s | 328.22 | Viscous... |
| D*i | 0.00 | m2/s | 328.25 | Viscous... |
| D*i | 0.00 | m2/s | 333.14 | Viscous... |
| D*i | 0.00 | m2/s | 337.93 | Viscous... |
| D*i | 0.00 | m2/s | 337.97 | Viscous... |
| D*i | 0.00 | m2/s | 337.99 | Viscous... |
| D*i | 0.00 | m2/s | 348.08 | Viscous... |
| D*i | 0.00 | m2/s | 352.75 | Viscous... |
| D*i | 0.00 | m2/s | 352.77 | Viscous... |
| D*i | 0.00 | m2/s | 364.53 | Viscous... |
| D*i | 0.00 | m2/s | 364.54 | Viscous... |
| ΔfusS | [138.80; 139.75] | J/mol×K | [263.50; 263.59] |
|
| ΔfusS | 138.80 | J/mol×K | 263.50 | NIST |
| ΔfusS | 139.75 | J/mol×K | 263.59 | NIST |
| γ | [0.02; 0.03] | N/m | [293.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.03 300 310 320 | ||||
| γ | 0.02 | N/m | 293.15 | Density... |
| γ | 0.02 | N/m | 293.15 | Surface... |
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 294.10 | Density... |
| γ | 0.02 | N/m | 298.15 | Interfa... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 303.15 | Interfa... |
| γ | 0.02 | N/m | 303.15 | Density... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
| λ | [0.13; 0.14] | W/m×K | [318.20; 352.80] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.13 0.13 0.13 0.13 320 330 340 350 | ||||
| λ | 0.14 | W/m×K | 318.20 | Thermal... |
| λ | 0.13 | W/m×K | 323.20 | Thermal... |
| λ | 0.13 | W/m×K | 328.10 | Thermal... |
| λ | 0.13 | W/m×K | 333.10 | Thermal... |
| λ | 0.13 | W/m×K | 337.70 | Thermal... |
| λ | 0.13 | W/m×K | 343.20 | Thermal... |
| λ | 0.13 | W/m×K | 347.90 | Thermal... |
| λ | 0.13 | W/m×K | 352.80 | Thermal... |
| αdiff | [4.25e-08; 5.83e-08] | m2/s | [423.73; 523.18] |
|
|
T(K) Thermal diffusivity (m2/s) 4.50e-8 5.00e-8 5.50e-8 450 500 | ||||
| αdiff | 5.83e-08 | m2/s | 423.73 | Thermal... |
| αdiff | 5.23e-08 | m2/s | 448.23 | Thermal... |
| αdiff | 4.87e-08 | m2/s | 473.10 | Thermal... |
| αdiff | 4.58e-08 | m2/s | 498.16 | Thermal... |
| αdiff | 4.25e-08 | m2/s | 523.18 | Thermal... |
Datasets
- Molar heat capacity at constant pressure, J/K/mol (1)
- Viscosity, Pa*s (3)
- Mass density, kg/m3 (9)
- Speed of sound, m/s (1)
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 323.15 | 100.00 | 386.32 |
| 328.15 | 100.00 | 389.56 |
| 333.15 | 100.00 | 392.79 |
| 338.15 | 100.00 | 395.86 |
| 343.15 | 100.00 | 399.09 |
| 348.15 | 100.00 | 402.33 |
| 353.15 | 100.00 | 405.57 |
| 358.15 | 100.00 | 408.80 |
| 363.15 | 100.00 | 412.04 |
| 368.15 | 100.00 | 415.28 |
| 373.15 | 100.00 | 418.85 |
| 378.15 | 100.00 | 422.09 |
| 383.15 | 100.00 | 425.50 |
| 388.15 | 100.00 | 428.73 |
| 393.15 | 100.00 | 432.31 |
| 398.15 | 100.00 | 435.38 |
| 403.15 | 100.00 | 438.78 |
| 408.15 | 100.00 | 442.53 |
| 413.15 | 100.00 | 445.77 |
| 418.15 | 100.00 | 449.34 |
| 423.15 | 100.00 | 452.92 |
| 428.15 | 100.00 | 456.50 |
| 433.15 | 100.00 | 460.59 |
| 438.15 | 100.00 | 465.35 |
| 323.15 | 10180.00 | 385.13 |
| 328.15 | 10180.00 | 388.02 |
| 333.15 | 10180.00 | 391.26 |
| 338.15 | 10180.00 | 394.33 |
| 343.15 | 10180.00 | 397.39 |
| 348.15 | 10180.00 | 400.46 |
| 353.15 | 10180.00 | 403.52 |
| 358.15 | 10180.00 | 406.93 |
| 363.15 | 10180.00 | 410.00 |
| 368.15 | 10180.00 | 413.23 |
| 373.15 | 10180.00 | 416.13 |
| 378.15 | 10180.00 | 419.36 |
| 383.15 | 10180.00 | 422.60 |
| 388.15 | 10180.00 | 426.01 |
| 393.15 | 10180.00 | 429.07 |
| 398.15 | 10180.00 | 433.16 |
| 403.15 | 10180.00 | 435.89 |
| 408.15 | 10180.00 | 438.78 |
| 413.15 | 10180.00 | 441.68 |
| 418.15 | 10180.00 | 444.06 |
| 423.15 | 10180.00 | 447.64 |
| 428.15 | 10180.00 | 450.88 |
| 433.15 | 10180.00 | 454.28 |
| 438.15 | 10180.00 | 458.20 |
| 443.15 | 10180.00 | 462.12 |
| 448.15 | 10180.00 | 465.70 |
| 453.15 | 10180.00 | 469.95 |
| Reference | ||
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 100.00 | 0.0015 |
| 293.15 | 1000.00 | 0.0015 |
| 293.15 | 5000.00 | 0.0016 |
| 293.15 | 10000.00 | 0.0017 |
| 293.15 | 20000.00 | 0.0019 |
| 293.15 | 30000.00 | 0.0021 |
| 293.15 | 40000.00 | 0.0023 |
| 293.15 | 50000.00 | 0.0026 |
| 293.15 | 60000.00 | 0.0028 |
| 293.15 | 70000.00 | 0.0031 |
| 293.15 | 80000.00 | 0.0034 |
| 293.15 | 100000.00 | 0.0041 |
| 293.15 | 120000.00 | 0.0050 |
| 293.15 | 140000.00 | 0.0058 |
| 313.15 | 100.00 | 0.0011 |
| 313.15 | 1000.00 | 0.0011 |
| 313.15 | 5000.00 | 0.0011 |
| 313.15 | 10000.00 | 0.0012 |
| 313.15 | 20000.00 | 0.0013 |
| 313.15 | 30000.00 | 0.0015 |
| 313.15 | 40000.00 | 0.0016 |
| 313.15 | 50000.00 | 0.0018 |
| 313.15 | 60000.00 | 0.0019 |
| 313.15 | 70000.00 | 0.0021 |
| 313.15 | 80000.00 | 0.0023 |
| 313.15 | 100000.00 | 0.0028 |
| 313.15 | 120000.00 | 0.0032 |
| 313.15 | 140000.00 | 0.0038 |
| 333.15 | 100.00 | 0.0008 |
| 333.15 | 1000.00 | 0.0008 |
| 333.15 | 5000.00 | 0.0009 |
| 333.15 | 10000.00 | 0.0009 |
| 333.15 | 20000.00 | 0.0010 |
| 333.15 | 30000.00 | 0.0011 |
| 333.15 | 40000.00 | 0.0012 |
| 333.15 | 50000.00 | 0.0013 |
| 333.15 | 60000.00 | 0.0014 |
| 333.15 | 70000.00 | 0.0016 |
| 333.15 | 80000.00 | 0.0017 |
| 333.15 | 100000.00 | 0.0020 |
| 333.15 | 120000.00 | 0.0023 |
| 333.15 | 140000.00 | 0.0027 |
| 353.15 | 100.00 | 0.0006 |
| 353.15 | 1000.00 | 0.0006 |
| 353.15 | 5000.00 | 0.0007 |
| 353.15 | 10000.00 | 0.0007 |
| 353.15 | 20000.00 | 0.0008 |
| 353.15 | 30000.00 | 0.0009 |
| 353.15 | 40000.00 | 0.0010 |
| 353.15 | 50000.00 | 0.0010 |
| 353.15 | 60000.00 | 0.0011 |
| 353.15 | 70000.00 | 0.0012 |
| 353.15 | 80000.00 | 0.0013 |
| 353.15 | 100000.00 | 0.0015 |
| 353.15 | 120000.00 | 0.0018 |
| 353.15 | 140000.00 | 0.0020 |
| 373.15 | 100.00 | 0.0005 |
| 373.15 | 1000.00 | 0.0005 |
| 373.15 | 5000.00 | 0.0005 |
| 373.15 | 10000.00 | 0.0006 |
| 373.15 | 20000.00 | 0.0006 |
| 373.15 | 30000.00 | 0.0007 |
| 373.15 | 40000.00 | 0.0008 |
| 373.15 | 50000.00 | 0.0008 |
| 373.15 | 60000.00 | 0.0009 |
| 373.15 | 70000.00 | 0.0010 |
| 373.15 | 80000.00 | 0.0011 |
| 373.15 | 100000.00 | 0.0012 |
| 373.15 | 120000.00 | 0.0014 |
| 373.15 | 140000.00 | 0.0016 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.20 | 6020.00 | 0.0015 |
| 298.20 | 8050.00 | 0.0015 |
| 298.20 | 10020.00 | 0.0015 |
| 304.90 | 6020.00 | 0.0013 |
| 303.40 | 8050.00 | 0.0014 |
| 303.30 | 10020.00 | 0.0014 |
| 314.50 | 5990.00 | 0.0011 |
| 313.40 | 8000.00 | 0.0012 |
| 313.30 | 10020.00 | 0.0012 |
| 323.40 | 6050.00 | 0.0010 |
| 323.10 | 8010.00 | 0.0010 |
| 323.40 | 10000.00 | 0.0010 |
| 334.10 | 6010.00 | 0.0009 |
| 333.30 | 8030.00 | 0.0009 |
| 333.40 | 10000.00 | 0.0009 |
| 343.30 | 5990.00 | 0.0008 |
| 343.20 | 8070.00 | 0.0008 |
| 343.30 | 10010.00 | 0.0008 |
| 353.40 | 6080.00 | 0.0007 |
| 353.60 | 8020.00 | 0.0007 |
| 353.40 | 9980.00 | 0.0007 |
| 364.00 | 6040.00 | 0.0006 |
| 363.70 | 8020.00 | 0.0006 |
| 363.30 | 10050.00 | 0.0006 |
| 374.00 | 6000.00 | 0.0005 |
| 373.90 | 8020.00 | 0.0006 |
| 373.10 | 10070.00 | 0.0006 |
| 383.00 | 6010.00 | 0.0005 |
| 383.40 | 8050.00 | 0.0005 |
| 383.20 | 10000.00 | 0.0005 |
| 393.10 | 6080.00 | 0.0005 |
| 393.60 | 8030.00 | 0.0005 |
| 393.00 | 10020.00 | 0.0005 |
| 403.00 | 6040.00 | 0.0004 |
| 404.10 | 8020.00 | 0.0004 |
| 403.10 | 10040.00 | 0.0004 |
| 413.20 | 6080.00 | 0.0004 |
| 413.70 | 7990.00 | 0.0004 |
| 412.90 | 10010.00 | 0.0004 |
| 423.00 | 6080.00 | 0.0004 |
| 423.90 | 8050.00 | 0.0004 |
| 423.40 | 10000.00 | 0.0004 |
| 433.20 | 6010.00 | 0.0003 |
| 433.30 | 8000.00 | 0.0003 |
| 432.90 | 10020.00 | 0.0004 |
| 443.50 | 6020.00 | 0.0003 |
| 443.50 | 8010.00 | 0.0003 |
| 443.20 | 10050.00 | 0.0003 |
| 453.30 | 6020.00 | 0.0003 |
| 454.00 | 8040.00 | 0.0003 |
| 453.30 | 9950.00 | 0.0003 |
| 463.40 | 6040.00 | 0.0003 |
| 464.10 | 8020.00 | 0.0003 |
| 463.30 | 10010.00 | 0.0003 |
| 473.40 | 6040.00 | 0.0003 |
| 473.50 | 8010.00 | 0.0003 |
| 473.30 | 10050.00 | 0.0003 |
| 483.40 | 6050.00 | 0.0002 |
| 483.40 | 8080.00 | 0.0002 |
| 483.40 | 10000.00 | 0.0002 |
| 493.40 | 6040.00 | 0.0002 |
| 493.40 | 8010.00 | 0.0002 |
| 493.20 | 10050.00 | 0.0002 |
| 503.40 | 6080.00 | 0.0002 |
| 502.70 | 7960.00 | 0.0002 |
| 503.20 | 10010.00 | 0.0002 |
| 514.20 | 6050.00 | 0.0002 |
| 513.00 | 8040.00 | 0.0002 |
| 513.00 | 10000.00 | 0.0002 |
| 523.70 | 5970.00 | 0.0002 |
| 523.00 | 8000.00 | 0.0002 |
| 523.70 | 10040.00 | 0.0002 |
| 533.50 | 6040.00 | 0.0002 |
| 533.30 | 8040.00 | 0.0002 |
| 533.50 | 10070.00 | 0.0002 |
| 542.90 | 6010.00 | 0.0002 |
| 542.90 | 8060.00 | 0.0002 |
| 542.90 | 9950.00 | 0.0002 |
| 552.90 | 6070.00 | 0.0001 |
| 553.20 | 8010.00 | 0.0002 |
| 552.90 | 10020.00 | 0.0002 |
| 563.00 | 6050.00 | 0.0001 |
| 563.00 | 8020.00 | 0.0001 |
| 563.00 | 10020.00 | 0.0002 |
| 573.00 | 6010.00 | 0.0001 |
| 573.00 | 8020.00 | 0.0001 |
| 573.00 | 10040.00 | 0.0001 |
| 582.80 | 6000.00 | 0.0001 |
| 582.90 | 7960.00 | 0.0001 |
| 582.80 | 10010.00 | 0.0001 |
| 593.00 | 6020.00 | 0.0001 |
| 592.90 | 8070.00 | 0.0001 |
| 593.00 | 10000.00 | 0.0001 |
| 603.10 | 6010.00 | 0.0001 |
| 602.90 | 8020.00 | 0.0001 |
| 603.10 | 10010.00 | 0.0001 |
| 613.10 | 6040.00 | 0.0001 |
| 612.90 | 8020.00 | 0.0001 |
| 613.10 | 10010.00 | 0.0001 |
| 623.20 | 6050.00 | 0.0001 |
| 623.00 | 7990.00 | 0.0001 |
| 623.20 | 10050.00 | 0.0001 |
| 633.50 | 6020.00 | 0.0001 |
| 632.80 | 8040.00 | 0.0001 |
| 633.50 | 10010.00 | 0.0001 |
| 643.40 | 6020.00 | 0.0001 |
| 643.00 | 8050.00 | 0.0001 |
| 643.40 | 10010.00 | 0.0001 |
| 653.40 | 6070.00 | 0.0001 |
| 652.90 | 8020.00 | 0.0001 |
| 653.40 | 10040.00 | 0.0001 |
| 663.20 | 6010.00 | 0.0001 |
| 663.10 | 8010.00 | 0.0001 |
| 663.20 | 10050.00 | 0.0001 |
| 673.50 | 6040.00 | 0.0001 |
| 672.90 | 8010.00 | 0.0001 |
| 673.50 | 9980.00 | 0.0001 |
| 683.30 | 6010.00 | 0.0001 |
| 683.20 | 8050.00 | 0.0001 |
| 683.20 | 10040.00 | 0.0001 |
| 693.20 | 6010.00 | 0.0001 |
| 693.20 | 8020.00 | 0.0001 |
| 693.20 | 10010.00 | 0.0001 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 284.60 | 670.00 | 0.0018 |
| 284.70 | 2710.00 | 0.0018 |
| 284.70 | 4240.00 | 0.0018 |
| 350.50 | 690.00 | 0.0007 |
| 350.50 | 4250.00 | 0.0007 |
| 350.50 | 8310.00 | 0.0007 |
| 294.00 | 8310.00 | 0.0016 |
| 322.30 | 4240.00 | 0.0010 |
| 284.60 | 2190.00 | 0.0018 |
| 353.10 | 8320.00 | 0.0007 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.09 | 1022.00 | 735.79 |
| 313.09 | 2023.00 | 736.6 |
| 313.09 | 3017.00 | 737.36 |
| 313.09 | 4026.00 | 738.14 |
| 313.09 | 5023.00 | 738.89 |
| 313.09 | 6032.00 | 739.66 |
| 313.09 | 7011.00 | 740.38 |
| 313.09 | 8009.00 | 741.15 |
| 313.09 | 9026.00 | 741.91 |
| 313.09 | 10008.00 | 742.66 |
| 313.09 | 11022.00 | 743.39 |
| 313.09 | 12012.00 | 744.09 |
| 313.09 | 13019.00 | 744.82 |
| 313.09 | 14017.00 | 745.55 |
| 313.09 | 15025.00 | 746.22 |
| 313.09 | 16025.00 | 746.91 |
| 313.09 | 17015.00 | 747.58 |
| 313.09 | 18022.00 | 748.26 |
| 313.09 | 19025.00 | 748.93 |
| 313.09 | 20013.00 | 749.59 |
| 313.09 | 21015.00 | 750.23 |
| 313.09 | 22011.00 | 750.9 |
| 313.09 | 23021.00 | 751.53 |
| 313.09 | 24015.00 | 752.21 |
| 313.09 | 24354.00 | 752.42 |
| 322.97 | 1025.00 | 728.33 |
| 322.97 | 2028.00 | 729.17 |
| 322.97 | 3026.00 | 729.97 |
| 322.97 | 4034.00 | 730.78 |
| 322.97 | 5021.00 | 731.59 |
| 322.97 | 6017.00 | 732.37 |
| 322.97 | 7017.00 | 733.17 |
| 322.97 | 8041.00 | 733.99 |
| 322.97 | 9015.00 | 734.73 |
| 322.97 | 10016.00 | 735.5 |
| 322.97 | 11019.00 | 736.28 |
| 322.97 | 12011.00 | 737.01 |
| 322.97 | 13028.00 | 737.78 |
| 322.97 | 14041.00 | 738.53 |
| 322.97 | 14994.00 | 739.22 |
| 322.97 | 16027.00 | 739.96 |
| 322.97 | 17001.00 | 740.64 |
| 322.97 | 18015.00 | 741.35 |
| 322.97 | 19032.00 | 742.07 |
| 322.97 | 20004.00 | 742.74 |
| 322.97 | 21009.00 | 743.43 |
| 322.97 | 22023.00 | 744.14 |
| 322.97 | 23009.00 | 744.8 |
| 322.97 | 24013.00 | 745.5 |
| 322.97 | 24507.00 | 745.83 |
| 332.80 | 1023.00 | 721.08 |
| 332.80 | 2019.00 | 721.96 |
| 332.80 | 3022.00 | 722.81 |
| 332.80 | 4030.00 | 723.69 |
| 332.80 | 5026.00 | 724.53 |
| 332.80 | 6035.00 | 725.36 |
| 332.80 | 7014.00 | 726.16 |
| 332.80 | 8025.00 | 727.03 |
| 332.80 | 9017.00 | 727.84 |
| 332.80 | 10020.00 | 728.67 |
| 332.80 | 11023.00 | 729.46 |
| 332.80 | 12022.00 | 730.26 |
| 332.80 | 13004.00 | 731.04 |
| 332.80 | 14008.00 | 731.81 |
| 332.80 | 15018.00 | 732.57 |
| 332.80 | 16023.00 | 733.35 |
| 332.80 | 17014.00 | 734.08 |
| 332.80 | 18006.00 | 734.82 |
| 332.80 | 19024.00 | 735.59 |
| 332.80 | 20023.00 | 736.32 |
| 332.80 | 21009.00 | 737.01 |
| 332.80 | 22009.00 | 737.73 |
| 332.80 | 23018.00 | 738.45 |
| 332.80 | 24018.00 | 739.17 |
| 332.80 | 24665.00 | 739.63 |
| 342.69 | 1019.00 | 713.8 |
| 342.69 | 2025.00 | 714.75 |
| 342.69 | 3025.00 | 715.67 |
| 342.69 | 4014.00 | 716.58 |
| 342.69 | 5015.00 | 717.47 |
| 342.69 | 6017.00 | 718.36 |
| 342.69 | 7021.00 | 719.25 |
| 342.69 | 8007.00 | 720.13 |
| 342.69 | 9019.00 | 721.03 |
| 342.69 | 10018.00 | 721.86 |
| 342.69 | 11016.00 | 722.71 |
| 342.69 | 12013.00 | 723.56 |
| 342.69 | 13021.00 | 724.39 |
| 342.69 | 14020.00 | 725.21 |
| 342.69 | 15030.00 | 726.04 |
| 342.69 | 16024.00 | 726.83 |
| 342.69 | 17011.00 | 727.58 |
| 342.69 | 18025.00 | 728.36 |
| 342.69 | 19023.00 | 729.15 |
| 342.69 | 20013.00 | 729.88 |
| 342.69 | 21006.00 | 730.67 |
| 342.69 | 22021.00 | 731.41 |
| 342.69 | 23014.00 | 732.15 |
| 342.69 | 24013.00 | 732.89 |
| 342.69 | 24725.00 | 733.44 |
| 352.51 | 1021.00 | 706.54 |
| 352.51 | 2027.00 | 707.55 |
| 352.51 | 3013.00 | 708.48 |
| 352.51 | 4019.00 | 709.46 |
| 352.51 | 5027.00 | 710.45 |
| 352.51 | 6014.00 | 711.35 |
| 352.51 | 7020.00 | 712.33 |
| 352.51 | 8000.00 | 713.23 |
| 352.51 | 9024.00 | 714.18 |
| 352.51 | 10009.00 | 715.07 |
| 352.51 | 11022.00 | 715.96 |
| 352.51 | 12012.00 | 716.84 |
| 352.51 | 13026.00 | 717.71 |
| 352.51 | 14017.00 | 718.6 |
| 352.51 | 15021.00 | 719.45 |
| 352.51 | 16022.00 | 720.3 |
| 352.51 | 17012.00 | 721.08 |
| 352.51 | 18027.00 | 721.95 |
| 352.51 | 19013.00 | 722.74 |
| 352.51 | 20028.00 | 723.53 |
| 352.51 | 21021.00 | 724.33 |
| 352.51 | 22023.00 | 725.14 |
| 352.51 | 23008.00 | 725.88 |
| 352.51 | 24020.00 | 726.65 |
| 352.51 | 24813.00 | 727.31 |
| 362.29 | 1015.00 | 699.21 |
| 362.29 | 2020.00 | 700.31 |
| 362.29 | 3015.00 | 701.33 |
| 362.29 | 4012.00 | 702.34 |
| 362.29 | 5029.00 | 703.4 |
| 362.29 | 6009.00 | 704.36 |
| 362.29 | 7029.00 | 705.38 |
| 362.29 | 8013.00 | 706.3 |
| 362.29 | 9012.00 | 707.31 |
| 362.29 | 10038.00 | 708.31 |
| 362.29 | 11027.00 | 709.22 |
| 362.29 | 12009.00 | 710.09 |
| 362.29 | 13007.00 | 711.04 |
| 362.29 | 14015.00 | 711.96 |
| 362.29 | 15008.00 | 712.81 |
| 362.29 | 16034.00 | 713.71 |
| 362.29 | 17030.00 | 714.59 |
| 362.29 | 18011.00 | 715.43 |
| 362.29 | 19021.00 | 716.29 |
| 362.29 | 20007.00 | 717.15 |
| 362.29 | 21017.00 | 717.94 |
| 362.29 | 22032.00 | 718.77 |
| 362.29 | 23002.00 | 719.6 |
| 362.29 | 24005.00 | 720.38 |
| 362.29 | 24809.00 | 721.05 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 745.23 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.00 | 2100.00 | 752.3 |
| 293.00 | 3100.00 | 752.9 |
| 293.00 | 4100.00 | 753.6 |
| 293.00 | 5000.00 | 754.2 |
| 293.00 | 10100.00 | 757.5 |
| 293.00 | 20000.00 | 763.5 |
| 293.00 | 30000.00 | 769.0 |
| 293.00 | 40000.00 | 774.3 |
| 293.00 | 50000.00 | 779.0 |
| 293.00 | 60000.00 | 783.8 |
| 293.00 | 69900.00 | 788.0 |
| 293.00 | 79900.00 | 792.5 |
| 293.00 | 89900.00 | 796.7 |
| 293.00 | 99900.00 | 800.8 |
| 293.00 | 109900.00 | 804.8 |
| 293.00 | 119900.00 | 808.7 |
| 293.00 | 129900.00 | 812.4 |
| 293.00 | 134900.00 | 814.4 |
| 293.00 | 137400.00 | 815.2 |
| 313.00 | 2100.00 | 737.7 |
| 313.00 | 3100.00 | 738.5 |
| 313.00 | 4100.00 | 739.2 |
| 313.00 | 5000.00 | 739.9 |
| 313.00 | 10100.00 | 743.4 |
| 313.00 | 20000.00 | 750.1 |
| 313.00 | 30000.00 | 756.3 |
| 313.00 | 40000.00 | 761.8 |
| 313.00 | 50000.00 | 767.1 |
| 313.00 | 60000.00 | 772.1 |
| 313.00 | 69900.00 | 777.0 |
| 313.00 | 79900.00 | 781.6 |
| 313.00 | 89900.00 | 786.1 |
| 313.00 | 99900.00 | 790.4 |
| 313.00 | 109900.00 | 794.6 |
| 313.00 | 119900.00 | 798.7 |
| 313.00 | 129900.00 | 802.7 |
| 313.00 | 134900.00 | 804.6 |
| 313.00 | 137400.00 | 805.4 |
| 333.00 | 2100.00 | 722.8 |
| 333.00 | 3100.00 | 723.6 |
| 333.00 | 4100.00 | 724.5 |
| 333.00 | 5000.00 | 725.3 |
| 333.00 | 10100.00 | 729.4 |
| 333.00 | 20000.00 | 736.6 |
| 333.00 | 30000.00 | 743.4 |
| 333.00 | 40000.00 | 749.6 |
| 333.00 | 50000.00 | 755.3 |
| 333.00 | 60000.00 | 760.8 |
| 333.00 | 69900.00 | 766.0 |
| 333.00 | 79900.00 | 770.9 |
| 333.00 | 89900.00 | 775.7 |
| 333.00 | 99900.00 | 780.1 |
| 333.00 | 109900.00 | 784.6 |
| 333.00 | 119900.00 | 788.8 |
| 333.00 | 129900.00 | 793.2 |
| 333.00 | 134900.00 | 795.1 |
| 333.00 | 137400.00 | 796.0 |
| 353.00 | 2100.00 | 708.1 |
| 353.00 | 3100.00 | 709.0 |
| 353.00 | 4100.00 | 710.0 |
| 353.00 | 5000.00 | 710.9 |
| 353.00 | 10100.00 | 715.6 |
| 353.00 | 20000.00 | 723.9 |
| 353.00 | 30000.00 | 731.3 |
| 353.00 | 40000.00 | 737.7 |
| 353.00 | 50000.00 | 744.1 |
| 353.00 | 60000.00 | 750.1 |
| 353.00 | 69900.00 | 755.6 |
| 353.00 | 79900.00 | 760.7 |
| 353.00 | 89900.00 | 765.7 |
| 353.00 | 99900.00 | 770.5 |
| 353.00 | 109900.00 | 775.1 |
| 353.00 | 119900.00 | 779.6 |
| 353.00 | 129900.00 | 784.0 |
| 353.00 | 134900.00 | 786.0 |
| 353.00 | 137400.00 | 787.0 |
| 373.00 | 2100.00 | 693.2 |
| 373.00 | 3100.00 | 694.3 |
| 373.00 | 4100.00 | 695.3 |
| 373.00 | 5000.00 | 696.3 |
| 373.00 | 10100.00 | 701.5 |
| 373.00 | 20000.00 | 710.8 |
| 373.00 | 30000.00 | 718.7 |
| 373.00 | 40000.00 | 726.0 |
| 373.00 | 50000.00 | 733.1 |
| 373.00 | 60000.00 | 739.4 |
| 373.00 | 69900.00 | 745.2 |
| 373.00 | 79900.00 | 750.7 |
| 373.00 | 89900.00 | 756.0 |
| 373.00 | 99900.00 | 761.0 |
| 373.00 | 109900.00 | 765.9 |
| 373.00 | 119900.00 | 770.6 |
| 373.00 | 129900.00 | 775.1 |
| 373.00 | 134900.00 | 777.4 |
| 373.00 | 137400.00 | 778.5 |
| 393.00 | 2100.00 | 678.1 |
| 393.00 | 3100.00 | 679.2 |
| 393.00 | 4100.00 | 680.4 |
| 393.00 | 5000.00 | 681.6 |
| 393.00 | 10100.00 | 687.5 |
| 393.00 | 20000.00 | 697.8 |
| 393.00 | 30000.00 | 706.6 |
| 393.00 | 40000.00 | 714.7 |
| 393.00 | 50000.00 | 722.2 |
| 393.00 | 60000.00 | 728.7 |
| 393.00 | 69900.00 | 735.1 |
| 393.00 | 79900.00 | 741.1 |
| 393.00 | 89900.00 | 746.8 |
| 393.00 | 99900.00 | 752.2 |
| 393.00 | 109900.00 | 757.2 |
| 393.00 | 119900.00 | 762.0 |
| 393.00 | 129900.00 | 766.8 |
| 393.00 | 134900.00 | 769.0 |
| 393.00 | 137400.00 | 770.2 |
| 413.00 | 2100.00 | 662.8 |
| 413.00 | 3100.00 | 664.2 |
| 413.00 | 4100.00 | 665.6 |
| 413.00 | 5000.00 | 666.9 |
| 413.00 | 10100.00 | 673.7 |
| 413.00 | 20000.00 | 685.1 |
| 413.00 | 30000.00 | 694.9 |
| 413.00 | 40000.00 | 703.6 |
| 413.00 | 50000.00 | 711.4 |
| 413.00 | 60000.00 | 718.7 |
| 413.00 | 69900.00 | 725.4 |
| 413.00 | 79900.00 | 731.7 |
| 413.00 | 89900.00 | 737.3 |
| 413.00 | 99900.00 | 743.2 |
| 413.00 | 109900.00 | 748.5 |
| 413.00 | 119900.00 | 753.7 |
| 413.00 | 129900.00 | 758.5 |
| 413.00 | 134900.00 | 760.9 |
| 413.00 | 137400.00 | 762.0 |
| 433.00 | 2100.00 | 646.8 |
| 433.00 | 3100.00 | 648.5 |
| 433.00 | 4100.00 | 650.0 |
| 433.00 | 5000.00 | 651.6 |
| 433.00 | 10100.00 | 659.5 |
| 433.00 | 20000.00 | 672.0 |
| 433.00 | 30000.00 | 682.8 |
| 433.00 | 40000.00 | 692.1 |
| 433.00 | 50000.00 | 700.6 |
| 433.00 | 60000.00 | 708.3 |
| 433.00 | 69900.00 | 715.6 |
| 433.00 | 79900.00 | 722.1 |
| 433.00 | 89900.00 | 728.3 |
| 433.00 | 99900.00 | 734.3 |
| 433.00 | 109900.00 | 739.8 |
| 433.00 | 119900.00 | 745.1 |
| 433.00 | 129900.00 | 750.3 |
| 433.00 | 134900.00 | 752.7 |
| 433.00 | 137400.00 | 753.9 |
| 448.00 | 2100.00 | 634.6 |
| 448.00 | 3100.00 | 636.7 |
| 448.00 | 4100.00 | 638.2 |
| 448.00 | 5000.00 | 640.0 |
| 448.00 | 10100.00 | 648.5 |
| 448.00 | 20000.00 | 662.4 |
| 448.00 | 30000.00 | 674.0 |
| 448.00 | 40000.00 | 684.0 |
| 448.00 | 50000.00 | 692.9 |
| 448.00 | 60000.00 | 701.0 |
| 448.00 | 69900.00 | 708.3 |
| 448.00 | 79900.00 | 715.3 |
| 448.00 | 89900.00 | 721.9 |
| 448.00 | 99900.00 | 727.9 |
| 448.00 | 109900.00 | 733.5 |
| 448.00 | 119900.00 | 739.0 |
| 448.00 | 129900.00 | 744.2 |
| 448.00 | 134900.00 | 746.7 |
| 448.00 | 137400.00 | 747.9 |
| 468.00 | 2100.00 | 617.8 |
| 468.00 | 3100.00 | 619.9 |
| 468.00 | 4100.00 | 622.0 |
| 468.00 | 5000.00 | 624.1 |
| 468.00 | 10100.00 | 634.1 |
| 468.00 | 20000.00 | 649.5 |
| 468.00 | 30000.00 | 661.8 |
| 468.00 | 40000.00 | 672.8 |
| 468.00 | 50000.00 | 682.6 |
| 468.00 | 60000.00 | 691.0 |
| 468.00 | 69900.00 | 698.9 |
| 468.00 | 79900.00 | 706.3 |
| 468.00 | 89900.00 | 712.9 |
| 468.00 | 99900.00 | 719.2 |
| 468.00 | 109900.00 | 725.1 |
| 468.00 | 119900.00 | 731.0 |
| 468.00 | 129900.00 | 736.3 |
| 468.00 | 134900.00 | 738.9 |
| 468.00 | 137400.00 | 740.2 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.29 | 100.00 | 756.0 |
| 283.29 | 1000.00 | 757.0 |
| 283.29 | 3000.00 | 758.0 |
| 283.30 | 5000.00 | 760.0 |
| 283.30 | 10000.00 | 763.0 |
| 283.31 | 20000.00 | 769.0 |
| 283.30 | 30000.00 | 775.0 |
| 283.30 | 40000.00 | 780.0 |
| 283.30 | 50000.00 | 785.0 |
| 283.30 | 60000.00 | 790.0 |
| 283.31 | 70000.00 | 795.0 |
| 283.32 | 80000.00 | 799.0 |
| 283.32 | 90000.00 | 803.0 |
| 293.17 | 100.00 | 749.0 |
| 293.18 | 1000.00 | 750.0 |
| 293.19 | 5000.00 | 753.0 |
| 293.19 | 10000.00 | 756.0 |
| 293.19 | 20000.00 | 763.0 |
| 293.19 | 30000.00 | 769.0 |
| 293.19 | 40000.00 | 774.0 |
| 293.19 | 50000.00 | 780.0 |
| 293.20 | 60000.00 | 785.0 |
| 293.19 | 70000.00 | 789.0 |
| 293.19 | 80000.00 | 794.0 |
| 293.19 | 90000.00 | 798.0 |
| 293.19 | 100000.00 | 802.0 |
| 303.05 | 100.00 | 742.0 |
| 303.05 | 1000.00 | 743.0 |
| 303.05 | 5000.00 | 746.0 |
| 303.06 | 10000.00 | 749.0 |
| 303.05 | 20000.00 | 756.0 |
| 303.04 | 30000.00 | 762.0 |
| 303.06 | 40000.00 | 768.0 |
| 303.05 | 50000.00 | 774.0 |
| 303.05 | 60000.00 | 779.0 |
| 303.05 | 70000.00 | 784.0 |
| 303.05 | 80000.00 | 789.0 |
| 303.05 | 90000.00 | 793.0 |
| 303.04 | 100000.00 | 797.0 |
| 312.89 | 100.00 | 736.0 |
| 312.89 | 1000.00 | 737.0 |
| 312.90 | 5000.00 | 740.0 |
| 312.90 | 10000.00 | 744.0 |
| 312.90 | 20000.00 | 751.0 |
| 312.90 | 30000.00 | 757.0 |
| 312.90 | 40000.00 | 763.0 |
| 312.90 | 50000.00 | 769.0 |
| 312.90 | 60000.00 | 774.0 |
| 312.90 | 70000.00 | 780.0 |
| 312.90 | 80000.00 | 784.0 |
| 312.90 | 90000.00 | 789.0 |
| 312.90 | 100000.00 | 793.0 |
| 322.83 | 100.00 | 727.0 |
| 322.83 | 1000.00 | 728.0 |
| 322.83 | 5000.00 | 732.0 |
| 322.83 | 10000.00 | 736.0 |
| 322.83 | 20000.00 | 743.0 |
| 322.83 | 30000.00 | 750.0 |
| 322.83 | 40000.00 | 756.0 |
| 322.83 | 50000.00 | 762.0 |
| 322.83 | 60000.00 | 768.0 |
| 322.83 | 70000.00 | 773.0 |
| 322.83 | 80000.00 | 778.0 |
| 322.83 | 90000.00 | 783.0 |
| 322.83 | 100000.00 | 787.0 |
| 332.74 | 100.00 | 720.0 |
| 332.74 | 1000.00 | 721.0 |
| 332.74 | 5000.00 | 725.0 |
| 332.74 | 10000.00 | 729.0 |
| 332.74 | 20000.00 | 737.0 |
| 332.74 | 30000.00 | 744.0 |
| 332.74 | 40000.00 | 750.0 |
| 332.74 | 50000.00 | 757.0 |
| 332.74 | 60000.00 | 762.0 |
| 332.74 | 70000.00 | 768.0 |
| 332.74 | 80000.00 | 773.0 |
| 332.74 | 90000.00 | 778.0 |
| 332.75 | 100000.00 | 782.0 |
| 342.67 | 100.00 | 713.0 |
| 342.67 | 1000.00 | 714.0 |
| 342.67 | 5000.00 | 718.0 |
| 342.67 | 10000.00 | 722.0 |
| 342.67 | 20000.00 | 731.0 |
| 342.67 | 30000.00 | 738.0 |
| 342.67 | 40000.00 | 745.0 |
| 342.67 | 50000.00 | 751.0 |
| 342.67 | 60000.00 | 757.0 |
| 342.67 | 69990.00 | 763.0 |
| 342.67 | 80000.00 | 768.0 |
| 342.67 | 90000.00 | 773.0 |
| 342.67 | 100000.00 | 778.0 |
| 352.58 | 100.00 | 707.0 |
| 352.58 | 1000.00 | 708.0 |
| 352.58 | 5000.00 | 712.0 |
| 352.58 | 10000.00 | 716.0 |
| 352.58 | 20000.00 | 725.0 |
| 352.58 | 30000.00 | 733.0 |
| 352.58 | 40000.00 | 740.0 |
| 352.58 | 50000.00 | 747.0 |
| 352.58 | 60000.00 | 753.0 |
| 352.58 | 70000.00 | 759.0 |
| 352.58 | 80000.00 | 764.0 |
| 352.58 | 90000.00 | 769.0 |
| 352.58 | 100000.00 | 774.0 |
| 362.49 | 100.00 | 699.0 |
| 362.49 | 1000.00 | 700.0 |
| 362.48 | 5000.00 | 704.0 |
| 362.48 | 10000.00 | 709.0 |
| 362.48 | 20000.00 | 718.0 |
| 362.48 | 30000.00 | 726.0 |
| 362.49 | 40000.00 | 734.0 |
| 362.48 | 50000.00 | 741.0 |
| 362.49 | 60000.00 | 747.0 |
| 362.49 | 70000.00 | 753.0 |
| 362.48 | 80000.00 | 759.0 |
| 362.48 | 90000.00 | 764.0 |
| 362.49 | 100000.00 | 769.0 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 759.2 |
| 278.15 | 1000.00 | 760.5 |
| 278.15 | 5000.00 | 763.1 |
| 278.15 | 10000.00 | 766.2 |
| 278.15 | 20000.00 | 771.9 |
| 278.15 | 30000.00 | 777.3 |
| 278.15 | 40000.00 | 782.3 |
| 278.15 | 50000.00 | 787.1 |
| 278.15 | 60000.00 | 791.7 |
| 298.15 | 100.00 | 745.6 |
| 298.15 | 1000.00 | 746.2 |
| 298.15 | 5000.00 | 749.0 |
| 298.15 | 10000.00 | 752.4 |
| 298.15 | 20000.00 | 758.7 |
| 298.15 | 30000.00 | 764.7 |
| 298.15 | 40000.00 | 770.1 |
| 298.15 | 50000.00 | 775.3 |
| 298.15 | 60000.00 | 780.2 |
| 323.15 | 100.00 | 727.2 |
| 323.15 | 1000.00 | 728.2 |
| 323.15 | 5000.00 | 731.4 |
| 323.15 | 10000.00 | 735.3 |
| 323.15 | 20000.00 | 742.6 |
| 323.15 | 30000.00 | 749.2 |
| 323.15 | 40000.00 | 755.2 |
| 323.15 | 50000.00 | 760.9 |
| 323.15 | 60000.00 | 766.3 |
| 348.15 | 100.00 | 708.7 |
| 348.15 | 1000.00 | 709.6 |
| 348.15 | 5000.00 | 713.4 |
| 348.15 | 10000.00 | 717.8 |
| 348.15 | 20000.00 | 726.1 |
| 348.15 | 30000.00 | 733.5 |
| 348.15 | 40000.00 | 740.2 |
| 348.15 | 50000.00 | 746.4 |
| 348.15 | 60000.00 | 752.3 |
| 373.15 | 1000.00 | 690.8 |
| 373.15 | 5000.00 | 695.2 |
| 373.15 | 10000.00 | 700.4 |
| 373.15 | 20000.00 | 709.8 |
| 373.15 | 30000.00 | 718.1 |
| 373.15 | 40000.00 | 725.6 |
| 373.15 | 50000.00 | 732.5 |
| 373.15 | 60000.00 | 738.9 |
| 423.15 | 1000.00 | 652.6 |
| 423.15 | 5000.00 | 658.7 |
| 423.15 | 10000.00 | 665.6 |
| 423.15 | 20000.00 | 677.6 |
| 423.15 | 30000.00 | 688.0 |
| 423.15 | 40000.00 | 697.0 |
| 423.15 | 50000.00 | 705.3 |
| 423.15 | 60000.00 | 712.8 |
| 463.15 | 5000.00 | 627.9 |
| 463.15 | 10000.00 | 636.9 |
| 463.15 | 20000.00 | 651.8 |
| 463.15 | 30000.00 | 664.2 |
| 463.15 | 40000.00 | 674.8 |
| 463.15 | 50000.00 | 684.1 |
| 463.15 | 60000.00 | 692.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.21 | 2007.00 | 750.58 |
| 293.21 | 3977.00 | 752.18 |
| 293.21 | 5979.00 | 753.71 |
| 293.21 | 7982.00 | 755.06 |
| 293.22 | 9987.00 | 756.38 |
| 293.21 | 12987.00 | 758.27 |
| 293.22 | 15986.00 | 760.07 |
| 293.22 | 18994.00 | 761.82 |
| 293.22 | 21995.00 | 763.63 |
| 293.22 | 24987.00 | 765.5 |
| 293.22 | 27987.00 | 767.37 |
| 293.21 | 29985.00 | 768.5 |
| 313.10 | 1990.00 | 736.16 |
| 313.10 | 4017.00 | 737.72 |
| 313.10 | 6016.00 | 739.14 |
| 313.10 | 8014.00 | 740.64 |
| 313.10 | 10011.00 | 742.11 |
| 313.10 | 13007.00 | 744.26 |
| 313.10 | 16011.00 | 746.36 |
| 313.10 | 19017.00 | 748.61 |
| 313.10 | 22017.00 | 750.69 |
| 313.10 | 25019.00 | 752.63 |
| 313.10 | 28017.00 | 754.52 |
| 313.10 | 30020.00 | 755.75 |
| 333.01 | 2024.00 | 721.82 |
| 333.00 | 3976.00 | 723.61 |
| 333.01 | 5981.00 | 725.32 |
| 333.01 | 7987.00 | 726.99 |
| 333.01 | 10019.00 | 728.35 |
| 333.01 | 13016.00 | 730.73 |
| 333.01 | 16014.00 | 733.04 |
| 333.01 | 19018.00 | 735.29 |
| 333.01 | 22015.00 | 737.46 |
| 333.01 | 25018.00 | 739.58 |
| 333.01 | 28015.00 | 741.65 |
| 333.01 | 30024.00 | 742.99 |
| 353.12 | 2000.00 | 706.86 |
| 353.12 | 3991.00 | 708.83 |
| 353.12 | 5996.00 | 710.75 |
| 353.12 | 8009.00 | 712.81 |
| 353.12 | 10014.00 | 714.63 |
| 353.12 | 13006.00 | 717.28 |
| 353.12 | 16007.00 | 719.83 |
| 353.12 | 19003.00 | 722.16 |
| 353.12 | 22006.00 | 724.55 |
| 353.12 | 25008.00 | 726.87 |
| 353.12 | 28011.00 | 729.13 |
| 353.12 | 30007.00 | 730.59 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 745.29 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.53 | 8012.00 | 740.43 |
| 313.50 | 9962.00 | 741.88 |
| 313.50 | 12011.00 | 743.35 |
| 313.52 | 13987.00 | 744.76 |
| 313.48 | 16030.00 | 746.15 |
| 313.48 | 17972.00 | 747.51 |
| 323.46 | 7994.00 | 733.56 |
| 323.48 | 9968.00 | 735.18 |
| 323.57 | 11960.00 | 736.57 |
| 323.52 | 13993.00 | 738.13 |
| 323.49 | 16021.00 | 739.64 |
| 323.49 | 18018.00 | 741.06 |
| 333.55 | 8003.00 | 726.32 |
| 333.51 | 9996.00 | 727.99 |
| 333.55 | 11980.00 | 729.56 |
| 333.56 | 13998.00 | 731.15 |
| 333.53 | 15975.00 | 732.68 |
| 333.52 | 17973.00 | 734.22 |
| 343.50 | 7959.00 | 719.25 |
| 343.50 | 10036.00 | 721.04 |
| 343.48 | 11000.00 | 721.9 |
| 343.48 | 11993.00 | 722.72 |
| 343.47 | 12998.00 | 723.59 |
| 343.52 | 13977.00 | 724.32 |
| 343.54 | 14989.00 | 725.15 |
| 343.55 | 15979.00 | 725.97 |
| 343.56 | 16970.00 | 726.72 |
| 343.56 | 18004.00 | 727.54 |
| 353.57 | 8022.00 | 712.16 |
| 353.57 | 10035.00 | 713.95 |
| 353.58 | 11021.00 | 714.86 |
| 353.58 | 12000.00 | 715.73 |
| 353.56 | 13021.00 | 716.67 |
| 353.56 | 13976.00 | 717.47 |
| 353.52 | 15037.00 | 718.45 |
| 353.55 | 15991.00 | 719.22 |
| 353.59 | 17027.00 | 720.07 |
| 353.53 | 17993.00 | 720.9 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 756.0 |
| 100.00 | 288.15 | 752.4 |
| 100.00 | 293.15 | 748.8 |
| 100.00 | 298.15 | 745.3 |
| 100.00 | 303.15 | 741.7 |
| 100.00 | 308.15 | 738.1 |
| 100.00 | 313.15 | 734.4 |
| 100.00 | 318.15 | 730.8 |
| 100.00 | 323.15 | 727.1 |
| 10000.00 | 283.15 | 762.4 |
| 10000.00 | 288.15 | 758.9 |
| 10000.00 | 293.15 | 755.5 |
| 10000.00 | 298.15 | 752.1 |
| 10000.00 | 303.15 | 748.7 |
| 10000.00 | 308.15 | 745.3 |
| 10000.00 | 313.15 | 741.8 |
| 10000.00 | 318.15 | 738.4 |
| 10000.00 | 323.15 | 734.9 |
| 20000.00 | 283.15 | 768.3 |
| 20000.00 | 288.15 | 765.1 |
| 20000.00 | 293.15 | 761.7 |
| 20000.00 | 298.15 | 758.5 |
| 20000.00 | 303.15 | 755.2 |
| 20000.00 | 308.15 | 752.0 |
| 20000.00 | 313.15 | 748.7 |
| 20000.00 | 318.15 | 745.4 |
| 20000.00 | 323.15 | 742.0 |
| 30000.00 | 283.15 | 773.9 |
| 30000.00 | 288.15 | 770.7 |
| 30000.00 | 293.15 | 767.6 |
| 30000.00 | 298.15 | 764.4 |
| 30000.00 | 303.15 | 761.3 |
| 30000.00 | 308.15 | 758.2 |
| 30000.00 | 313.15 | 755.0 |
| 30000.00 | 318.15 | 751.9 |
| 30000.00 | 323.15 | 748.6 |
| 40000.00 | 283.15 | 779.2 |
| 40000.00 | 288.15 | 776.1 |
| 40000.00 | 293.15 | 773.1 |
| 40000.00 | 298.15 | 770.0 |
| 40000.00 | 303.15 | 767.0 |
| 40000.00 | 308.15 | 764.0 |
| 40000.00 | 313.15 | 760.9 |
| 40000.00 | 318.15 | 757.9 |
| 40000.00 | 323.15 | 754.8 |
| 50000.00 | 283.15 | 784.1 |
| 50000.00 | 288.15 | 781.2 |
| 50000.00 | 293.15 | 778.2 |
| 50000.00 | 298.15 | 775.3 |
| 50000.00 | 303.15 | 772.4 |
| 50000.00 | 308.15 | 769.4 |
| 50000.00 | 313.15 | 766.4 |
| 50000.00 | 318.15 | 763.5 |
| 50000.00 | 323.15 | 760.5 |
| 60000.00 | 283.15 | 788.6 |
| 60000.00 | 288.15 | 786.0 |
| 60000.00 | 293.15 | 783.2 |
| 60000.00 | 298.15 | 780.3 |
| 60000.00 | 303.15 | 777.5 |
| 60000.00 | 308.15 | 774.6 |
| 60000.00 | 313.15 | 771.7 |
| 60000.00 | 318.15 | 768.8 |
| 60000.00 | 323.15 | 765.9 |
| Reference | ||
Speed of sound, m/s
Operational condition: Frequency, MHz = 3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 10000.00 | 303.15 | 1318.5 |
| 20000.00 | 303.15 | 1372.4 |
| 30000.00 | 303.15 | 1421.4 |
| 40000.00 | 303.15 | 1468.5 |
| 50000.00 | 303.15 | 1512.3 |
| 60000.00 | 303.15 | 1553.7 |
| 70000.00 | 303.15 | 1593.3 |
| 10000.00 | 313.15 | 1281.7 |
| 20000.00 | 313.15 | 1337.9 |
| 30000.00 | 313.15 | 1389.6 |
| 40000.00 | 313.15 | 1436.8 |
| 50000.00 | 313.15 | 1481.5 |
| 60000.00 | 313.15 | 1524.2 |
| 70000.00 | 313.15 | 1564.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [6.62e-04; 1746.95] | kPa | [263.57; 658.20] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.12723e+02 | |||
| Coefficient B | -1.12005e+04 | |||
| Coefficient C | -1.39838e+01 | |||
| Coefficient D | 5.78857e-06 | |||
| Temperature range, min. | 263.57 | |||
| Temperature range, max. | 658.20 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 300 400 500 600 | ||||
| Pvap | 6.62e-04 | kPa | 263.57 | Calculated Property |
| Pvap | 0.04 | kPa | 307.42 | Calculated Property |
| Pvap | 0.66 | kPa | 351.27 | Calculated Property |
| Pvap | 5.30 | kPa | 395.11 | Calculated Property |
| Pvap | 25.51 | kPa | 438.96 | Calculated Property |
| Pvap | 86.39 | kPa | 482.81 | Calculated Property |
| Pvap | 228.37 | kPa | 526.66 | Calculated Property |
| Pvap | 505.56 | kPa | 570.50 | Calculated Property |
| Pvap | 984.52 | kPa | 614.35 | Calculated Property |
| Pvap | 1746.95 | kPa | 658.20 | Calculated Property |
Similar Compounds
Find more compounds similar to Dodecane.
Mixtures
- Dodecane + Ethyl Acetate
- Dodecane + Isopropyl acetate
- Dodecane + 2-Pyrrolidinone, 1-methyl-
- Dodecane + 2-Pyrrolidinone, 1-methyl- + Benzene, propyl-
- Dodecane + Formamide, N,N-dimethyl-
- Dodecane + Formamide, N,N-dimethyl- + Benzene, (1-methylpropyl)-
- Dodecane + o-Toluidine
- Benzo[b]thiophene + Dodecane
- 1-Propanol + Dodecane
- Dodecane + Tributyl phosphate
- 1-Octanamine, N,N-dioctyl- + Dodecane
- Dodecane + Benzaldehyde
- Carbon dioxide + Dodecane
- Acetonitrile + Dodecane + Acetic acid
- Acetonitrile + Dodecane + Propanoic acid
- Acetonitrile + Dodecane + Butanoic acid
- Acetonitrile + Dodecane + Propanoic acid, 2-methyl-
- Acetonitrile + Dodecane + Pentanoic acid
- Acetonitrile + Dodecane + Butanoic acid, 3-methyl-
- Dodecane + Acetophenone
Find more mixtures with Dodecane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
- Liquid liquid equilibria for n-alkanes (C12, C14, C17) + propylbenzene +NMP mixtures at temperatures between 298 and 328K
- Phase equilibria for the extraction of sec-butylbenzene from dodecane with N,N-dimethylformamide
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
- High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
- Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
- Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
- Ionic liquids on desulfurization of fuel oils
- Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
- Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
- P-x data for binary systems using a novel static total pressure apparatus
- Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
- Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
- Liquid-liquid equilibria for ternary systems acetic acid + n-butylacetate + hydrocarbons at 293.15 K
- Interfacial tension of binary mixtures exhibiting azeotropic behavior: Measurement and modeling with PCP-SAFT combined with Density Gradient Theory
- Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Liquid liquid equilibria measurements of ternary systems (acetonitrile + a carboxylic acid + dodecane) at 303.15 K
- Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
- Speed of sound and thermodynamic properties of ternary liquid mixture octane + dodecane + hexadecane
- High pressure phase behaviour of the CO2 + 1-decanol + n-dodecane system
- Liquid-liquid-liquid equilibria for water + [P6 6 6 14][DCA] + dodecane ternary system
- Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
- Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
- An experimental investigation on the solubility of methane in 1-octanol and n-dodecane at ambient temperatures
- Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
- Compressed liquid densities of binary mixtures of n-decane + n-dodecane at temperatures from 283 K to 363 K and pressures up to 100 MPa
- High temperature and pressure water/oil interfacial tension benchmark data for the Ninth Industrial Fluid Properties Simulation Challenge
- Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
- Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
- Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
- Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
- Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
- Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether +2-methylpentane + (n-decane or n-dodecane) at the temperature 298.15 K
- Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
- Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
- Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
- (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
- Ternary (liquid + liquid) equilibria for mixtures of (methanol + aniline + n-octane or n-dodecane) at T = 298.15 K
- (Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
- Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
- Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
- Thermodynamic and acoustic properties of (heptane + dodecane) mixtures under elevated pressures
- Partition behaviour of benzoic acid in (water + n-dodecane) solutions at T = (293.15 and 298.15) K
- Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
- Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
- Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
- Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
- (Liquid + liquid) equilibria for the ternary system (water + dodecane + propylene glycol n-propyl ether)
- Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
- Evaluation of [bmim][PF6] as an ionic solvent for the extraction of propylbenzene from aliphatic compounds
- Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
- Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
- Water/oil/[P6,6,6,14][NTf2] phase equilibria
- (Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
- Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
- Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
- Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
- Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
- Phase equilibrium measurements and thermodynamic modeling of binary mixtures containing a diesel compound n-dodecane + biodiesel compounds: Ethyl dodecanoate and ethyl octanoate
- Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
- Thermophysical properties of fatty acid methyl and ethyl esters
- Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
- Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
- Viscous Calibration Liquids for Self-diffusion Measurements
- Prediction and Experimental Measurement of Refractive Index in Ternary Hydrocarbon Mixtures
- Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
- Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
- Densities of the binary systems n-hexane + n-decane and nhexane + n-hexadecane up to 60 MPa and 463 K
- Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)
- Liquid Liquid Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
- Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
- Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester
- Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
- Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
- Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
- Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
- Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
- Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
- Density, Viscosity, and Structure of Equilibrium Solvent Phases in Butyric Acid Extraction by Phosphonium Ionic Liquid
- Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
- Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
- Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
- Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
- Density and Compressibility of Multicomponent n-Alkane Mixtures up to 463 K and 140 MPa
- Viscosity Measurements of n-Dodecane at Temperatures between 303 K and 693 K and Pressures up to 10 MPa
- Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
- Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
- Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
- Liquid-Liquid Equilibria of Formic Acid and Furfural in a Biphasic Aqueous-Organic System: Optimization of Solvent and Amine Extractant
- Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- Liquid-Liquid Equilibria of Lactic Acid/Water Solutions in Tri-iso-octylamine/Dodecane/1-Dodecanol at 306.1, 310.1, and 316.1 K. Experimental Data and Prediction
- Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
- Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
- Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
- Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
- Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
- Liquid-Liquid Equilibrium for Ternary Systems of N-Methylformamide + Pyrrole/Indole + Alkanes at 298.15 K: Phase Equilibrium Measurement and Correlation
- Density, Speed of Sound, Compressibility, and Excess Properties of Carbon Dioxide + n-Dodecane Binary Mixtures from 10 to 70 MPa
- Experimental Investigation of the Thermophysical Properties of the Bio-Aviation Fuel Surrogates: Binary and Ternary Mixtures of n-Dodecane, Methyl Butyrate, and Methyl Decanoate
- Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
- Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
- Excess molar volumes and enthalpies of mixing for the ternary system (butyl butyrate + 1-octanol + dodecane) at the temperature 308.15 K.
- Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
- Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
- Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
- Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
- Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
- Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
- Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Measurement and Correlation of Phase Equilibria for Dodecane + sec-Butylbenzene + N-Methyl-2-pyrrolidone
- Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
- Vapor-Liquid Equilibria of Binary Systems of Ethene Oxide + Dodecane, Ethene Oxide + 1-Decanol, and Ethene Oxide + 1-Dodecanol and Prediction with the Predictive Soave-Redlich-Kwong (PSRK) Equation of State
- Liquid-Liquid Equilibria for {1-Ethyl-3-methylimidazolium Diethylphosphate or 1-Ethyl-3-methylimidazolium Ethylsulfate} + 4,6-Dimethyldibenzothiophene + Dodecane Systems at 298.2 K and 313.2 K
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Vapor-Liquid Equilibrium Data for the Nitrogen + Dodecane System at Temperatures from (344 to 593) K and at Pressures up to 60 MPa
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Liquid Liquid Equilibria of Alkane (C10 C14) + sec-Butylbenzene + Sulfolane
- Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
- Vapor Liquid Equilibria of Binary and Ternary Systems Containing Carbon Dioxide, Alkane, and Benzothiophene
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Liquid Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
- Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
- Liquid Liquid Equilibrium in N-Methyl-2-hydroxyethylammonium Acetate, Butanoate, or Hexanoate Ionic Liquids + Dibenzothiophene + n-Dodecane Systems at 298.2 K and Atmospheric Pressure
- Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
- Isothermal Vapor Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
- Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
- Extraction of Butylbenzene from Dodecane Using Hexafluorophosphate-Based Ionic Liquids: Effect of Cation Change
- Liquid Liquid Equilibria for the Ternary System Water + Dodecane + 1-(1-Methyl-2-propoxyethoxy)-2-propanol
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
- Density, Viscosity, and Interfacial Tension of Binary Mixture of Tri-iso-amyl Phosphate (TiAP) and n-Dodecane: Effect of Compositions and Gamma Absorbed Doses
- Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol
- Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
- Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa
- Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
- Measurement and Modeling of the Densities for CO2 + Dodecane System from 313.55 K to 353.55 K and Pressures up to 18 MPa
- Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
- Liquid-Liquid Equilibria of Alkane (C10-C14) + Hexylbenzene + Sulfolane
- Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
- Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
- Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
- Comparison between Experimental and Theoretical Estimations of the Thermal Expansion, Concentration Expansion Coefficients, and Viscosity for Binary Mixtures under Pressures up to 20 MPa
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Miscibility of Trihexyl(tetradecyl)phosphonium Chloride with Alkanes
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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