- Name
- Ethanol, 2-(ethylamino)-
- InChI
- InChI=1S/C4H11NO/c1-2-5-3-4-6/h5-6H,2-4H2,1H3
- InChI Key
- MIJDSYMOBYNHOT-UHFFFAOYSA-N
- Formula
- C4H11NO
- SMILES
- CCNCCO
- Mol. Weight (g/mol)
- 89.14
- CAS
- 110-73-6
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Datasets
- η - Viscosity, Pa*s (2)
- ν - Kinematic viscosity, m2/s
- n0 - Refractive index (Na D-line)
- ρl - Mass density, kg/m3 (3)
- γ - Surface tension liquid-gas, N/m
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0154 |
| 293.15 | 0.2000 | 0.0238 |
| 293.15 | 0.4000 | 0.0317 |
| 293.15 | 0.6000 | 0.0310 |
| 293.15 | 0.8000 | 0.0138 |
| 293.15 | 1.0000 | 0.0010 |
| 303.15 | 0.0000 | 0.0097 |
| 303.15 | 0.2000 | 0.0145 |
| 303.15 | 0.4000 | 0.0186 |
| 303.15 | 0.6000 | 0.0173 |
| 303.15 | 0.8000 | 0.0083 |
| 303.15 | 1.0000 | 0.0008 |
| 313.15 | 0.0000 | 0.0066 |
| 313.15 | 0.2000 | 0.0093 |
| 313.15 | 0.4000 | 0.0114 |
| 313.15 | 0.6000 | 0.0107 |
| 313.15 | 0.8000 | 0.0054 |
| 313.15 | 1.0000 | 0.0006 |
| 323.15 | 0.0000 | 0.0045 |
| 323.15 | 0.2000 | 0.0062 |
| 323.15 | 0.4000 | 0.0073 |
| 323.15 | 0.6000 | 0.0071 |
| 323.15 | 0.8000 | 0.0037 |
| 323.15 | 1.0000 | 0.0006 |
| 333.15 | 0.0000 | 0.0034 |
| 333.15 | 0.2000 | 0.0045 |
| 333.15 | 0.4000 | 0.0050 |
| 333.15 | 0.6000 | 0.0047 |
| 333.15 | 0.8000 | 0.0027 |
| 333.15 | 1.0000 | 0.0005 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of Ethanol, 2-(ethylamino)- (1) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 0.0890 | 293.15 | 0.0015 |
| 0.1780 | 293.15 | 0.0025 |
| 0.2670 | 293.15 | 0.0037 |
| 0.3560 | 293.15 | 0.0058 |
| 0.0890 | 298.15 | 0.0013 |
| 0.1780 | 298.15 | 0.0021 |
| 0.2670 | 298.15 | 0.0032 |
| 0.3560 | 298.15 | 0.0047 |
| 0.0890 | 303.15 | 0.0012 |
| 0.1780 | 303.15 | 0.0018 |
| 0.2670 | 303.15 | 0.0026 |
| 0.3560 | 303.15 | 0.0038 |
| 0.0890 | 308.15 | 0.0010 |
| 0.1780 | 308.15 | 0.0016 |
| 0.2670 | 308.15 | 0.0022 |
| 0.3560 | 308.15 | 0.0031 |
| 0.0890 | 313.15 | 0.0009 |
| 0.1780 | 313.15 | 0.0014 |
| 0.2670 | 313.15 | 0.0019 |
| 0.3560 | 313.15 | 0.0028 |
| 0.0890 | 318.15 | 0.0008 |
| 0.1780 | 318.15 | 0.0012 |
| 0.2670 | 318.15 | 0.0016 |
| 0.3560 | 318.15 | 0.0022 |
| 0.0890 | 323.15 | 0.0008 |
| 0.1780 | 323.15 | 0.0011 |
| 0.2670 | 323.15 | 0.0014 |
| 0.3560 | 323.15 | 0.0019 |
Kinematic viscosity, m2/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-(ethylamino)- (1) - Liquid | Kinematic viscosity, m2/s - Liquid |
| 298.15 | 0.5000 | 8.9763e-06 |
| 298.15 | 0.5004 | 8.9763e-06 |
| 298.15 | 0.5000 | 8.1909e-06 |
| 303.15 | 0.5000 | 7.1788e-06 |
| 303.15 | 0.5004 | 7.1788e-06 |
| 303.15 | 0.5000 | 7.1783e-06 |
| 303.15 | 0.5000 | 6.6143e-06 |
| 308.15 | 0.5000 | 5.7780e-06 |
| 308.15 | 0.5004 | 5.7780e-06 |
| 308.15 | 0.5000 | 5.4076e-06 |
| 313.15 | 0.5000 | 4.7394e-06 |
| 313.15 | 0.5004 | 4.7394e-06 |
| 313.15 | 0.5000 | 4.5443e-06 |
| 318.15 | 0.5000 | 3.9686e-06 |
| 318.15 | 0.5004 | 3.9686e-06 |
| 318.15 | 0.5000 | 3.8338e-06 |
| 323.15 | 0.5000 | 3.3436e-06 |
| 323.15 | 0.5004 | 3.3436e-06 |
| 323.15 | 0.5000 | 3.2360e-06 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of Ethanol, 2-(ethylamino)- (1) - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 0.0890 | 293.15 | 1.3453 |
| 0.1780 | 293.15 | 1.3591 |
| 0.2670 | 293.15 | 1.3705 |
| 0.3560 | 293.15 | 1.382 |
| 0.0890 | 298.15 | 1.3447 |
| 0.1780 | 298.15 | 1.3584 |
| 0.2670 | 298.15 | 1.3695 |
| 0.3560 | 298.15 | 1.3808 |
| 0.0890 | 303.15 | 1.3441 |
| 0.1780 | 303.15 | 1.3576 |
| 0.2670 | 303.15 | 1.3686 |
| 0.3560 | 303.15 | 1.3796 |
| 0.0890 | 308.15 | 1.3435 |
| 0.1780 | 308.15 | 1.3568 |
| 0.2670 | 308.15 | 1.3676 |
| 0.3560 | 308.15 | 1.3784 |
| 0.0890 | 313.15 | 1.3428 |
| 0.1780 | 313.15 | 1.356 |
| 0.2670 | 313.15 | 1.3666 |
| 0.3560 | 313.15 | 1.3772 |
| 0.0890 | 318.15 | 1.3422 |
| 0.1780 | 318.15 | 1.355 |
| 0.2670 | 318.15 | 1.3657 |
| 0.3560 | 318.15 | 1.3761 |
| 0.0890 | 323.15 | 1.3418 |
| 0.1780 | 323.15 | 1.3545 |
| 0.2670 | 323.15 | 1.3647 |
| 0.3560 | 323.15 | 1.3755 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 916.8 |
| 293.15 | 0.2000 | 929.5 |
| 293.15 | 0.4000 | 943.1 |
| 293.15 | 0.6000 | 961.6 |
| 293.15 | 0.8000 | 985.7 |
| 293.15 | 1.0000 | 998.0 |
| 303.15 | 0.0000 | 909.7 |
| 303.15 | 0.2000 | 922.4 |
| 303.15 | 0.4000 | 936.1 |
| 303.15 | 0.6000 | 954.8 |
| 303.15 | 0.8000 | 979.5 |
| 303.15 | 1.0000 | 995.1 |
| 313.15 | 0.0000 | 901.3 |
| 313.15 | 0.2000 | 914.0 |
| 313.15 | 0.4000 | 927.8 |
| 313.15 | 0.6000 | 946.0 |
| 313.15 | 0.8000 | 972.5 |
| 313.15 | 1.0000 | 992.2 |
| 323.15 | 0.0000 | 894.7 |
| 323.15 | 0.2000 | 907.4 |
| 323.15 | 0.4000 | 920.7 |
| 323.15 | 0.6000 | 938.7 |
| 323.15 | 0.8000 | 963.0 |
| 323.15 | 1.0000 | 989.2 |
| 333.15 | 0.0000 | 887.2 |
| 333.15 | 0.2000 | 898.6 |
| 333.15 | 0.4000 | 912.0 |
| 333.15 | 0.6000 | 931.1 |
| 333.15 | 0.8000 | 955.6 |
| 333.15 | 1.0000 | 985.0 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of Ethanol, 2-(ethylamino)- (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0890 | 293.15 | 996.48 |
| 0.1780 | 293.15 | 996.22 |
| 0.2670 | 293.15 | 996.54 |
| 0.3560 | 293.15 | 995.54 |
| 0.0890 | 298.15 | 995.09 |
| 0.1780 | 298.15 | 994.31 |
| 0.2670 | 298.15 | 994.09 |
| 0.3560 | 298.15 | 992.52 |
| 0.0890 | 303.15 | 993.47 |
| 0.1780 | 303.15 | 992.21 |
| 0.2670 | 303.15 | 991.47 |
| 0.3560 | 303.15 | 989.38 |
| 0.0890 | 308.15 | 991.64 |
| 0.1780 | 308.15 | 989.92 |
| 0.2670 | 308.15 | 988.72 |
| 0.3560 | 308.15 | 986.16 |
| 0.0890 | 313.15 | 989.61 |
| 0.1780 | 313.15 | 987.48 |
| 0.2670 | 313.15 | 985.86 |
| 0.3560 | 313.15 | 982.85 |
| 0.0890 | 318.15 | 987.4 |
| 0.1780 | 318.15 | 984.87 |
| 0.2670 | 318.15 | 982.87 |
| 0.3560 | 318.15 | 979.46 |
| 0.0890 | 323.15 | 985.02 |
| 0.1780 | 323.15 | 982.12 |
| 0.2670 | 323.15 | 979.77 |
| 0.3560 | 323.15 | 975.99 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-(ethylamino)- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.5000 | 984.792 |
| 298.15 | 0.5004 | 984.792 |
| 298.15 | 0.5000 | 1000.225 |
| 303.15 | 0.5000 | 981.056 |
| 303.15 | 0.5004 | 981.056 |
| 303.15 | 0.5000 | 996.84 |
| 308.15 | 0.5000 | 977.274 |
| 308.15 | 0.5004 | 977.274 |
| 308.15 | 0.5000 | 993.406 |
| 313.15 | 0.5000 | 973.445 |
| 313.15 | 0.5004 | 973.445 |
| 313.15 | 0.5000 | 989.916 |
| 318.15 | 0.5000 | 969.563 |
| 318.15 | 0.5004 | 969.563 |
| 318.15 | 0.5000 | 986.394 |
| 323.15 | 0.5000 | 965.63 |
| 323.15 | 0.5004 | 965.63 |
| 323.15 | 0.5000 | 982.806 |
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-(ethylamino)- (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 293.15 | 0.0000 | 0.0727 |
| 293.15 | 0.0104 | 0.0607 |
| 293.15 | 0.0220 | 0.0546 |
| 293.15 | 0.0482 | 0.0488 |
| 293.15 | 0.0795 | 0.0457 |
| 293.15 | 0.1189 | 0.0437 |
| 293.15 | 0.1679 | 0.0422 |
| 293.15 | 0.2292 | 0.0409 |
| 293.15 | 0.3064 | 0.0397 |
| 293.15 | 0.4252 | 0.0383 |
| 293.15 | 0.6476 | 0.0361 |
| 293.15 | 0.7929 | 0.0346 |
| 293.15 | 0.8852 | 0.0338 |
| 293.15 | 1.0000 | 0.0328 |
| 298.15 | 0.0000 | 0.0720 |
| 298.15 | 0.0104 | 0.0596 |
| 298.15 | 0.0220 | 0.0536 |
| 298.15 | 0.0482 | 0.0479 |
| 298.15 | 0.0795 | 0.0449 |
| 298.15 | 0.1189 | 0.0430 |
| 298.15 | 0.1679 | 0.0415 |
| 298.15 | 0.2292 | 0.0403 |
| 298.15 | 0.3064 | 0.0392 |
| 298.15 | 0.4252 | 0.0377 |
| 298.15 | 0.6476 | 0.0356 |
| 298.15 | 0.7929 | 0.0341 |
| 298.15 | 0.8852 | 0.0332 |
| 298.15 | 1.0000 | 0.0322 |
| 303.15 | 0.0000 | 0.0712 |
| 303.15 | 0.0104 | 0.0585 |
| 303.15 | 0.0220 | 0.0525 |
| 303.15 | 0.0482 | 0.0469 |
| 303.15 | 0.0795 | 0.0442 |
| 303.15 | 0.1189 | 0.0423 |
| 303.15 | 0.1679 | 0.0409 |
| 303.15 | 0.2292 | 0.0398 |
| 303.15 | 0.3064 | 0.0387 |
| 303.15 | 0.4252 | 0.0373 |
| 303.15 | 0.6476 | 0.0351 |
| 303.15 | 0.7929 | 0.0336 |
| 303.15 | 0.8852 | 0.0327 |
| 303.15 | 1.0000 | 0.0317 |
| 308.15 | 0.0000 | 0.0704 |
| 308.15 | 0.0104 | 0.0574 |
| 308.15 | 0.0220 | 0.0515 |
| 308.15 | 0.0482 | 0.0461 |
| 308.15 | 0.0795 | 0.0434 |
| 308.15 | 0.1189 | 0.0415 |
| 308.15 | 0.1679 | 0.0403 |
| 308.15 | 0.2292 | 0.0393 |
| 308.15 | 0.3064 | 0.0382 |
| 308.15 | 0.4252 | 0.0368 |
| 308.15 | 0.6476 | 0.0345 |
| 308.15 | 0.7929 | 0.0331 |
| 308.15 | 0.8852 | 0.0322 |
| 308.15 | 1.0000 | 0.0311 |
| 313.15 | 0.0000 | 0.0695 |
| 313.15 | 0.0104 | 0.0563 |
| 313.15 | 0.0220 | 0.0505 |
| 313.15 | 0.0482 | 0.0452 |
| 313.15 | 0.0795 | 0.0426 |
| 313.15 | 0.1189 | 0.0407 |
| 313.15 | 0.1679 | 0.0396 |
| 313.15 | 0.2292 | 0.0387 |
| 313.15 | 0.3064 | 0.0376 |
| 313.15 | 0.4252 | 0.0363 |
| 313.15 | 0.6476 | 0.0340 |
| 313.15 | 0.7929 | 0.0325 |
| 313.15 | 0.8852 | 0.0316 |
| 313.15 | 1.0000 | 0.0305 |
| 318.15 | 0.0000 | 0.0688 |
| 318.15 | 0.0104 | 0.0552 |
| 318.15 | 0.0220 | 0.0493 |
| 318.15 | 0.0482 | 0.0443 |
| 318.15 | 0.0795 | 0.0418 |
| 318.15 | 0.1189 | 0.0400 |
| 318.15 | 0.1679 | 0.0391 |
| 318.15 | 0.2292 | 0.0382 |
| 318.15 | 0.3064 | 0.0372 |
| 318.15 | 0.4252 | 0.0357 |
| 318.15 | 0.6476 | 0.0335 |
| 318.15 | 0.7929 | 0.0320 |
| 318.15 | 0.8852 | 0.0311 |
| 318.15 | 1.0000 | 0.0300 |
| 323.15 | 0.0000 | 0.0679 |
| 323.15 | 0.0104 | 0.0541 |
| 323.15 | 0.0220 | 0.0483 |
| 323.15 | 0.0482 | 0.0433 |
| 323.15 | 0.0795 | 0.0410 |
| 323.15 | 0.1189 | 0.0393 |
| 323.15 | 0.1679 | 0.0384 |
| 323.15 | 0.2292 | 0.0376 |
| 323.15 | 0.3064 | 0.0367 |
| 323.15 | 0.4252 | 0.0353 |
| 323.15 | 0.6476 | 0.0329 |
| 323.15 | 0.7929 | 0.0314 |
| 323.15 | 0.8852 | 0.0305 |
| 323.15 | 1.0000 | 0.0294 |
Sources
- Density and viscosity of monoethylethanolamine + H2O and monoethylethanolamine + diethylethanolamine solutions for CO2 capture
- Density, Viscosity, and Refractive Index of Aqueous CO2-Loaded and -Unloaded Ethylaminoethanol (EAE) Solutions from 293.15 to 323.15 K for Post Combustion CO2 Capture
- Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
- Surface Tension of Aqueous Binary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol and Aqueous Ternary Mixtures of These Amines with Triethanolamine or N-Methyldiethanolamine from (293.15 to 323.15) K
Note: These property values are available through the Cheméo API. A free account gives you an access key.