- InChI
- InChI=1S/C6H15N/c1-4-7(5-2)6-3/h4-6H2,1-3H3
- InChI Key
- ZMANZCXQSJIPKH-UHFFFAOYSA-N
- Formula
- C6H15N
- SMILES
- CCN(CC)CC
- Molecular Weight1
- 101.19
- CAS
- 121-44-8
- Other Names
-
- (C2H5)3N
- (Diethylamino)ethane
- 1069-58-5 (maleate)
- 554-68-7 (chloride)
- Ethanamine, N,N-diethyl-
- N,N,N-triethylamine
- N,N-DIETHYLETHANAMINE
- TEN
- Triaethylamin
- Trietilamina
- UN 1296
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- 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).
- Rg : Radius of Gyration.
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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.
- NFPA Health : NFPA Health 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.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- 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 | 0.3200 | KDB | |
| PAff | 981.80 | kJ/mol | NIST |
| BasG | 951.00 | kJ/mol | NIST |
| ΔcH°liquid | [-4377.09; -4354.30] | kJ/mol |
|
| ΔcH°liquid | -4377.09 ± 0.54 | kJ/mol | NIST |
| ΔcH°liquid | -4354.30 | kJ/mol | NIST |
| μ | 0.90 | debye | KDB |
| ΔfG° | 110.40 | kJ/mol | KDB |
| Rg | 3.9300 | KDB | |
| ΔfH°gas | [-143.10; -92.90] | kJ/mol |
|
| ΔfH°gas | -99.65 | kJ/mol | KDB |
| ΔfH°gas | -134.10 | kJ/mol | NIST |
| ΔfH°gas | -92.90 ± 0.50 | kJ/mol | NIST |
| ΔfH°gas | -143.10 | kJ/mol | NIST |
| ΔfH°liquid | [-178.00; -127.80] | kJ/mol |
|
| ΔfH°liquid | -169.00 | kJ/mol | NIST |
| ΔfH°liquid | -127.80 ± 0.54 | kJ/mol | NIST |
| ΔfH°liquid | -178.00 | kJ/mol | NIST |
| ΔfusH° | 14.32 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 30.99 | kJ/mol | Joback Calculated Property |
| IE | [7.10; 8.24] | eV |
|
| IE | 7.53 ± 0.10 | eV | NIST |
| IE | 7.47 ± 0.04 | eV | NIST |
| IE | 7.53 ± 0.10 | eV | NIST |
| IE | 7.30 | eV | NIST |
| IE | 7.10 ± 0.10 | eV | NIST |
| IE | 7.20 ± 0.09 | eV | NIST |
| IE | 7.84 | eV | NIST |
| IE | 7.50 ± 0.02 | eV | NIST |
| IE | 8.03 | eV | NIST |
| IE | 8.24 ± 0.04 | eV | NIST |
| IE | 8.08 | eV | NIST |
| IE | 8.19 ± 0.05 | eV | NIST |
| log10WS | -0.14 | Aq. Sol... | |
| logPoct/wat | 1.348 | Crippen Calculated Property | |
| McVol | 105.380 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 3032.00 | kPa | KDB |
| ρc | 257.02 ± 2.02 | kg/m3 | NIST |
| Inp | [672.00; 727.00] |
|
|
| Inp | 673.60 | NIST | |
| Inp | 673.60 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 711.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 684.00 | NIST | |
| I | [727.00; 812.40] |
|
|
| I | 812.40 | NIST | |
| I | 775.00 | NIST | |
| I | 774.00 | NIST | |
| I | 770.00 | NIST | |
| I | 775.00 | NIST | |
| I | 763.00 | NIST | |
| I | 780.00 | NIST | |
| I | Outlier 727.00 | NIST | |
| Tboil | 362.00 | K | KDB |
| Tc | 535.60 | K | KDB |
| Tfus | [158.00; 158.45] | K |
|
| Tfus | 158.40 | K | KDB |
| Tfus | 158.23 | K | Aq. Sol... |
| Tfus | 158.45 | K | NIST |
| Tfus | 158.45 ± 0.40 | K | NIST |
| Tfus | Outlier 158.00 ± 2.00 | K | NIST |
| Tfus | 158.45 ± 1.00 | K | NIST |
| Tfus | 158.40 ± 0.20 | K | NIST |
| Vc | 0.389 | m3/kmol | KDB |
| Zc | 0.2648510 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [183.89; 248.11] | J/mol×K | [349.12; 511.60] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 240 250 350 400 450 500 | ||||
| Cp,gas | 183.89 | J/mol×K | 349.12 | Joback Calculated Property |
| Cp,gas | 195.67 | J/mol×K | 376.20 | Joback Calculated Property |
| Cp,gas | 207.01 | J/mol×K | 403.28 | Joback Calculated Property |
| Cp,gas | 217.91 | J/mol×K | 430.36 | Joback Calculated Property |
| Cp,gas | 228.39 | J/mol×K | 457.44 | Joback Calculated Property |
| Cp,gas | 238.45 | J/mol×K | 484.52 | Joback Calculated Property |
| Cp,gas | 248.11 | J/mol×K | 511.60 | Joback Calculated Property |
| Cp,liquid | [177.00; 218.10] | J/mol×K | [298.00; 298.15] |
|
| Cp,liquid | 177.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 216.43 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 218.10 | J/mol×K | 298.15 | NIST |
| η | [0.0002980; 0.0004229] | Pa×s | [283.15; 323.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.00e-4 3.20e-4 3.40e-4 3.60e-4 3.80e-4 4.00e-4 4.20e-4 290 300 310 320 | ||||
| η | 0.0004229 | Pa×s | 283.15 | Dynamic... |
| η | 0.0004085 | Pa×s | 286.15 | Dynamic... |
| η | 0.0003989 | Pa×s | 288.15 | Dynamic... |
| η | 0.0003900 | Pa×s | 290.15 | Dynamic... |
| η | 0.0003855 | Pa×s | 291.15 | Dynamic... |
| η | 0.0003847 | Pa×s | 291.35 | Dynamic... |
| η | 0.0003660 | Pa×s | 298.15 | Thermod... |
| η | 0.0003400 | Pa×s | 303.15 | Thermod... |
| η | 0.0003340 | Pa×s | 308.15 | Thermod... |
| η | 0.0003310 | Pa×s | 313.15 | Thermod... |
| η | 0.0002980 | Pa×s | 323.15 | Thermod... |
| ΔvapH | [31.01; 35.20] | kJ/mol | [275.00; 363.30] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 31 32 33 34 35 300 350 | ||||
| ΔvapH | 35.20 ± 0.90 | kJ/mol | 275.00 | NIST |
| ΔvapH | 34.60 | kJ/mol | 311.00 | NIST |
| ΔvapH | 33.00 | kJ/mol | 311.00 | NIST |
| ΔvapH | 33.40 ± 0.20 | kJ/mol | 313.00 | NIST |
| ΔvapH | 33.90 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 34.10 | kJ/mol | 320.00 | NIST |
| ΔvapH | 33.00 ± 0.20 | kJ/mol | 328.00 | NIST |
| ΔvapH | 34.80 | kJ/mol | 332.00 | NIST |
| ΔvapH | 33.90 | kJ/mol | 336.00 | NIST |
| ΔvapH | 33.30 | kJ/mol | 340.50 | NIST |
| ΔvapH | 32.20 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 31.30 ± 0.20 | kJ/mol | 358.00 | NIST |
| ΔvapH | 31.01 | kJ/mol | 362.10 | NIST |
| ΔvapH | 31.38 | kJ/mol | 362.40 | KDB |
| ΔvapH | 33.18 | kJ/mol | 363.30 | NIST |
| Pvap | [2.46; 74.94] | kPa | [273.04; 352.77] |
|
|
T(K) Vapor pressure (kPa) 0 10 20 30 40 50 60 70 80 280 300 320 340 | ||||
| Pvap | 2.46 | kPa | 273.04 | Experim... |
| Pvap | 7.01 | kPa | 292.87 | Experim... |
| Pvap | 17.43 | kPa | 312.82 | Experim... |
| Pvap | 38.05 | kPa | 332.78 | Experim... |
| Pvap | 74.94 | kPa | 352.77 | Experim... |
| n0 | [1.38980; 1.40110] | [293.15; 318.15] |
|
|
|
T(K) Refractive Index 1.39 1.39 1.39 1.4 1.4 1.4 1.4 300 310 | ||||
| n0 | 1.39660 | 293.15 | Measure... | |
| n0 | 1.40110 | 298.15 | Densiti... | |
| n0 | 1.39920 | 298.15 | Density... | |
| n0 | 1.39830 | 298.15 | Density... | |
| n0 | 1.39830 | 303.15 | Densiti... | |
| n0 | 1.39580 | 303.15 | Density... | |
| n0 | 1.39550 | 303.15 | Density... | |
| n0 | 1.39500 | 308.15 | Densiti... | |
| n0 | 1.39260 | 308.15 | Density... | |
| n0 | 1.39290 | 308.15 | Density... | |
| n0 | 1.39280 | 313.15 | Densiti... | |
| n0 | 1.38980 | 318.15 | Densiti... | |
| ρl | [709.05; 732.03] | kg/m3 | [288.15; 313.15] |
|
|
T(K) Liquid Density (kg/m3) 710 715 720 725 730 290 300 310 | ||||
| ρl | 732.03 | kg/m3 | 288.15 | Volumet... |
| ρl | 728.00 | kg/m3 | 293.00 | KDB |
| ρl | 727.70 | kg/m3 | 293.15 | Volumet... |
| ρl | 727.40 | kg/m3 | 293.15 | Volumet... |
| ρl | 722.56 | kg/m3 | 298.15 | Excess ... |
| ρl | 722.77 | kg/m3 | 298.15 | Volumet... |
| ρl | 723.02 | kg/m3 | 298.15 | Volumet... |
| ρl | 723.01 | kg/m3 | 298.15 | Partial... |
| ρl | 722.81 | kg/m3 | 298.15 | Thermod... |
| ρl | 722.81 | kg/m3 | 298.15 | Thermod... |
| ρl | 718.12 | kg/m3 | 303.15 | Volumet... |
| ρl | 718.36 | kg/m3 | 303.15 | Volumet... |
| ρl | 718.44 | kg/m3 | 303.15 | Studies... |
| ρl | 718.44 | kg/m3 | 303.15 | Studies... |
| ρl | 718.44 | kg/m3 | 303.15 | Studies... |
| ρl | 713.65 | kg/m3 | 308.15 | Volumet... |
| ρl | 709.05 | kg/m3 | 313.15 | Studies... |
| csound,fluid | [1090.65; 1132.77] | m/s | [293.15; 303.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1090 1100 1110 1120 1130 295 300 | ||||
| csound,fluid | 1132.47 | m/s | 293.15 | Thermod... |
| csound,fluid | 1132.77 | m/s | 293.15 | Thermod... |
| csound,fluid | 1110.90 | m/s | 298.15 | Thermod... |
| csound,fluid | 1111.10 | m/s | 298.15 | Thermod... |
| csound,fluid | 1090.65 | m/s | 303.15 | Thermod... |
| csound,fluid | 1090.70 | m/s | 303.15 | Thermod... |
| γ | 0.02 | N/m | 293.20 | KDB |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Amount density, mol/m3 - Gas | Temperature, K - Gas | Viscosity, Pa*s - Gas |
| 2.2 | 299.67 | 6.4900e-06 |
| 2.2 | 299.85 | 6.4850e-06 |
| 2.2 | 313.96 | 6.7640e-06 |
| 2.2 | 326.63 | 7.0240e-06 |
| 2.2 | 339.05 | 7.2750e-06 |
| 2.2 | 352.50 | 7.5510e-06 |
| 2.2 | 366.60 | 7.8420e-06 |
| 2.2 | 381.14 | 8.1370e-06 |
| 2.2 | 394.56 | 8.4130e-06 |
| 2.2 | 409.20 | 8.7180e-06 |
| 2.2 | 422.79 | 8.9960e-06 |
| 2.2 | 437.42 | 9.2960e-06 |
| 2.2 | 451.72 | 9.5940e-06 |
| 2.2 | 466.58 | 9.9070e-06 |
| 2.2 | 480.36 | 0.0000 |
| 2.2 | 498.45 | 0.0000 |
| 3.13 | 300.02 | 6.4880e-06 |
| 3.13 | 303.12 | 6.5480e-06 |
| 3.13 | 316.33 | 6.8150e-06 |
| 3.13 | 324.26 | 6.9810e-06 |
| 3.13 | 338.31 | 7.2590e-06 |
| 3.13 | 352.91 | 7.5570e-06 |
| 3.13 | 366.49 | 7.8390e-06 |
| 3.13 | 380.67 | 8.1290e-06 |
| 3.13 | 394.95 | 8.4230e-06 |
| 3.13 | 412.99 | 8.8040e-06 |
| 3.13 | 423.41 | 9.0120e-06 |
| 3.13 | 437.51 | 9.3150e-06 |
| 3.13 | 451.74 | 9.5990e-06 |
| 3.13 | 469.98 | 9.9850e-06 |
| 3.13 | 480.86 | 0.0000 |
| 3.13 | 498.38 | 0.0000 |
| 4.2 | 296.98 | 6.4180e-06 |
| 4.2 | 297.97 | 6.4390e-06 |
| 4.2 | 310.02 | 6.6680e-06 |
| 4.2 | 324.95 | 6.9710e-06 |
| 4.2 | 338.63 | 7.2450e-06 |
| 4.2 | 353.30 | 7.5510e-06 |
| 4.2 | 365.86 | 7.8030e-06 |
| 4.2 | 385.41 | 8.2170e-06 |
| 4.2 | 394.25 | 8.3880e-06 |
| 4.2 | 409.73 | 8.7110e-06 |
| 4.2 | 423.93 | 8.9880e-06 |
| 4.2 | 436.97 | 9.2750e-06 |
| 4.2 | 451.76 | 9.5860e-06 |
| 4.2 | 466.71 | 9.8930e-06 |
| 4.2 | 481.32 | 0.0000 |
| 4.2 | 495.31 | 0.0000 |
| 4.99 | 297.98 | 6.4400e-06 |
| 4.99 | 298.33 | 6.4370e-06 |
| 4.99 | 314.61 | 6.7500e-06 |
| 4.99 | 325.84 | 6.9800e-06 |
| 4.99 | 338.25 | 7.2330e-06 |
| 4.99 | 352.46 | 7.5290e-06 |
| 4.99 | 367.25 | 7.8310e-06 |
| 4.99 | 380.54 | 8.1090e-06 |
| 4.99 | 394.51 | 8.3860e-06 |
| 4.99 | 409.32 | 8.7070e-06 |
| 4.99 | 423.25 | 8.9910e-06 |
| 4.99 | 437.62 | 9.2860e-06 |
| 4.99 | 451.28 | 9.5720e-06 |
| 4.99 | 466.45 | 9.8790e-06 |
| 4.99 | 480.43 | 0.0000 |
| 4.99 | 495.29 | 0.0000 |
| 6.31 | 297.59 | 6.4120e-06 |
| 6.31 | 299.36 | 6.4490e-06 |
| 6.31 | 310.29 | 6.6540e-06 |
| 6.31 | 324.90 | 6.9480e-06 |
| 6.31 | 337.84 | 7.2050e-06 |
| 6.31 | 352.41 | 7.4920e-06 |
| 6.31 | 366.77 | 7.7840e-06 |
| 6.31 | 381.83 | 8.1060e-06 |
| 6.31 | 394.49 | 8.3700e-06 |
| 6.31 | 408.97 | 8.6620e-06 |
| 6.31 | 423.92 | 8.9660e-06 |
| 6.31 | 437.11 | 9.2490e-06 |
| 6.31 | 451.66 | 9.5540e-06 |
| 6.31 | 465.92 | 9.8460e-06 |
| 6.31 | 481.09 | 0.0000 |
| 6.31 | 495.17 | 0.0000 |
| 7.52 | 299.24 | 6.4460e-06 |
| 7.52 | 326.04 | 6.9790e-06 |
| 7.52 | 338.12 | 7.2180e-06 |
| 7.52 | 352.32 | 7.5130e-06 |
| 7.52 | 366.72 | 7.8010e-06 |
| 7.52 | 385.75 | 8.2060e-06 |
| 7.52 | 394.86 | 8.3840e-06 |
| 7.52 | 409.67 | 8.6900e-06 |
| 7.52 | 423.03 | 8.9630e-06 |
| 7.52 | 437.87 | 9.2690e-06 |
| 7.52 | 451.93 | 9.5580e-06 |
| 7.52 | 471.39 | 9.9720e-06 |
| 7.52 | 480.70 | 0.0000 |
| 7.52 | 495.84 | 0.0000 |
| 8.75 | 297.87 | 6.4270e-06 |
| 8.75 | 300.11 | 6.4600e-06 |
| 8.75 | 311.78 | 6.6670e-06 |
| 8.75 | 324.05 | 6.9130e-06 |
| 8.75 | 338.92 | 7.2170e-06 |
| 8.75 | 352.34 | 7.4870e-06 |
| 8.75 | 366.42 | 7.7820e-06 |
| 8.75 | 381.06 | 8.0760e-06 |
| 8.75 | 395.11 | 8.3690e-06 |
| 8.75 | 408.35 | 8.6400e-06 |
| 8.75 | 422.67 | 8.9390e-06 |
| 8.75 | 437.76 | 9.2550e-06 |
| 8.75 | 451.45 | 9.5340e-06 |
| 8.75 | 466.63 | 9.8510e-06 |
| 8.75 | 480.12 | 0.0000 |
| 8.75 | 496.21 | 0.0000 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0003 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [275.55; 385.31] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.29590e+01 | |||
| Coefficient B | -2.11704e+03 | |||
| Coefficient C | -1.08476e+02 | |||
| Temperature range, min. | 275.55 | |||
| Temperature range, max. | 385.31 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 275.55 | Calculated Property |
| Pvap | 3.16 | kPa | 287.75 | Calculated Property |
| Pvap | 6.70 | kPa | 299.94 | Calculated Property |
| Pvap | 12.99 | kPa | 312.14 | Calculated Property |
| Pvap | 23.37 | kPa | 324.33 | Calculated Property |
| Pvap | 39.48 | kPa | 336.53 | Calculated Property |
| Pvap | 63.25 | kPa | 348.72 | Calculated Property |
| Pvap | 96.81 | kPa | 360.92 | Calculated Property |
| Pvap | 142.48 | kPa | 373.11 | Calculated Property |
| Pvap | 202.68 | kPa | 385.31 | Calculated Property |
| Pvap | [1.02e-05; 2785.21] | kPa | [158.45; 535.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.51266e+01 | |||
| Coefficient B | -6.12731e+03 | |||
| Coefficient C | -7.51862e+00 | |||
| Coefficient D | 5.20704e-06 | |||
| Temperature range, min. | 158.45 | |||
| Temperature range, max. | 535.15 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
| Pvap | 1.02e-05 | kPa | 158.45 | Calculated Property |
| Pvap | 6.09e-03 | kPa | 200.31 | Calculated Property |
| Pvap | 0.32 | kPa | 242.16 | Calculated Property |
| Pvap | 4.48 | kPa | 284.02 | Calculated Property |
| Pvap | 29.09 | kPa | 325.87 | Calculated Property |
| Pvap | 115.94 | kPa | 367.73 | Calculated Property |
| Pvap | 335.21 | kPa | 409.58 | Calculated Property |
| Pvap | 778.89 | kPa | 451.44 | Calculated Property |
| Pvap | 1554.27 | kPa | 493.29 | Calculated Property |
| Pvap | 2785.21 | kPa | 535.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Triethylamine.
Mixtures
- Benzene + Triethylamine
- n-Hexane + Triethylamine
- Ethanol + Triethylamine
- Triethylamine + 1-Butanol
- n-Hexane + Ethanol + Triethylamine
- n-Hexane + Triethylamine + 1-Butanol
- Triethylamine + Acetone
- 2-Butanone + Triethylamine
- 2-Pentanone + Triethylamine
- Triethylamine + 2-Heptanone
- Triethylamine + Water
- Trichloromethane + Triethylamine
- Triethylamine + Methyl Alcohol
- 1-Propanol + 2-Butanone + Triethylamine
- Acetonitrile + Triethylamine
- Triethylamine + 1,4-Dioxane
- Triethylamine + Ethyl Acetate
- Triethylamine + Acetic acid, butyl ester
- Benzene, chloro- + Triethylamine
- Benzene, nitro- + Triethylamine
Find more mixtures with Triethylamine.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Densities and Refractive Indices of Binary Mixtures of Benzene with Triethylamine and Tributylamine at Different Temperatures
- Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
- Thermodynamic properties of triethylamine +water liquid mixture from shear viscosity measurements
- The viscosity of triethylamine vapor at low densities and in the saturated vapor phase
- The viscosity of the binary vapor mixture methanol triethylamine at low densities and in the saturated vapor phase of the vapor liquid equilibrium
- Electrical conductivity investigation of diluted potassium chloride solutions in binary mixture triethylamine-water near its consolute point
- Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
- Measurement and correlation of the mutual solubility of diisopropylamine + water and triethylamine + water systems at high pressure
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
- Thermodynamic study of (heptane + amine) mixtures. III: Excess and partial molar volumes in mixtures with secondary, tertiary, and cyclic amines at 298.15 K
- Thermodynamics of (ketone + amine) mixtures. Part VI. Volumetric and speed of sound data at (293.15, 298.15, and 303.15) K for (2-heptanone + dipropylamine, +dibutylamine, or +triethylamine) systems
- Partial molar volume of tertiary amines in methanol at T = 298.15 K. Solvation, shape and specific interactions
- Thermodynamics of (ketone + amine) mixtures. Part XI. Excess molar enthalpies at T = 298.15 K for the (1-propanol + N,N,N-triethylamine + 2-butanone) system
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
- Volumetric and transport properties of ternary mixtures containing 1-propanol, triethylamine or tri-n-butylamine and cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents III. Alkylamines in butanols 303.15K
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents: IV. Alkylamines in 1,4-dioxane and oxolane at 303.15K
- Thermodynamics of ketone + amine mixtures Part IV. Volumetric and speed of sound data at (293.15; 298.15 and 303.15 K) for 2-butanone +dipropylamine, +dibutylamine or +triethylamine systems
- Thermodynamic study of Binary Mixtures of Tricyclo [5.2.1.0(2.6)] Decane with N-Methylpiperazine or Triethylamine at T = (298.15 to 323.15) K
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- 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
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Experimental Vapor Pressures of 2-Phenylethylamine, Benzylamine, Triethylamine, and cis-2,6-Dimethylpiperidine in the Range between 0.2 Pa and 75 kPa
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Dynamic Viscosity Study of Binary Mixtures Triethylamine + Water at Temperatures Ranging from (283.15 to 291.35) K
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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