![Ethanol, 2-[(2-aminoethyl)amino]-](data:image/png;base64, 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 "Ethanol, 2-[(2-aminoethyl)amino]-")
- Name
- Ethanol, 2-[(2-aminoethyl)amino]-
- InChI
- InChI=1S/C4H12N2O/c5-1-2-6-3-4-7/h6-7H,1-5H2
- InChI Key
- LHIJANUOQQMGNT-UHFFFAOYSA-N
- Formula
- C4H12N2O
- SMILES
- NCCNCCO
- Mol. Weight (g/mol)
- 104.15
- CAS
- 111-41-1
- 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
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Datasets
- Mass fraction (2)
- Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
- η - Viscosity, Pa*s (4)
- Excess molar enthalpy (molar enthalpy (4)
- Pvap - Vapor or sublimation pressure, kPa (2)
- n0 - Refractive index (Na D-line) (4)
- ρl - Mass density, kg/m3 (2)
- Tboil - Boiling temperature at pressure P, K (2)
Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) [ref]
Operational condition: Pressure, kPa = 86.66 (Liquid)
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Gas |
|---|---|
| 0.0580 | 0.0000 |
| 0.1010 | 0.0000 |
| 0.1500 | 0.0000 |
| 0.2440 | 0.0000 |
| 0.3530 | 0.0000 |
| 0.4340 | 0.0000 |
| 0.4830 | 0.0000 |
| 0.5380 | 0.0000 |
| 0.5740 | 0.0000 |
| 0.6070 | 0.0000 |
| 0.6590 | 0.0000 |
| 0.7050 | 0.0000 |
| 0.6900 | 0.0000 |
| 0.8860 | 0.0000 |
| 0.8840 | 0.0100 |
| 0.9700 | 0.3020 |
| 0.9800 | 0.9800 |
Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) [ref]
Operational condition: Pressure, kPa = 86.66 (Liquid)
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Gas |
|---|---|
| 0.0580 | 0.0000 |
| 0.1010 | 0.0000 |
| 0.1500 | 0.0000 |
| 0.2440 | 0.0000 |
| 0.3530 | 0.0000 |
| 0.4340 | 0.0000 |
| 0.4830 | 0.0000 |
| 0.5380 | 0.0000 |
| 0.5740 | 0.0000 |
| 0.6070 | 0.0000 |
| 0.6590 | 0.0000 |
| 0.7050 | 0.0000 |
| 0.6900 | 0.0000 |
| 0.8860 | 0.0000 |
| 0.8840 | 0.0100 |
| 0.9700 | 0.3020 |
| 0.9800 | 0.9800 |
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 303.15 | 0.0999 | 100.00 |
| 303.15 | 0.1999 | 121.00 |
| 303.15 | 0.2995 | 141.00 |
| 303.15 | 0.4000 | 161.00 |
| 303.15 | 0.5002 | 181.00 |
| 303.15 | 0.5997 | 201.00 |
| 303.15 | 0.7011 | 221.00 |
| 303.15 | 0.8003 | 240.00 |
| 303.15 | 0.8979 | 258.00 |
| 303.15 | 1.0000 | 279.00 |
| 308.15 | 0.0999 | 103.00 |
| 308.15 | 0.1999 | 125.00 |
| 308.15 | 0.2995 | 145.00 |
| 308.15 | 0.4000 | 165.00 |
| 308.15 | 0.5002 | 185.00 |
| 308.15 | 0.5997 | 205.00 |
| 308.15 | 0.7011 | 226.00 |
| 308.15 | 0.8003 | 245.00 |
| 308.15 | 0.8979 | 263.00 |
| 308.15 | 1.0000 | 284.00 |
| 313.15 | 0.0999 | 104.00 |
| 313.15 | 0.1999 | 127.00 |
| 313.15 | 0.2995 | 147.00 |
| 313.15 | 0.4000 | 167.00 |
| 313.15 | 0.5002 | 187.00 |
| 313.15 | 0.5997 | 207.00 |
| 313.15 | 0.7011 | 227.00 |
| 313.15 | 0.8003 | 247.00 |
| 313.15 | 0.8979 | 265.00 |
| 313.15 | 1.0000 | 285.00 |
| 318.15 | 0.0999 | 106.00 |
| 318.15 | 0.1999 | 129.00 |
| 318.15 | 0.2995 | 150.00 |
| 318.15 | 0.4000 | 170.00 |
| 318.15 | 0.5002 | 190.00 |
| 318.15 | 0.5997 | 209.00 |
| 318.15 | 0.7011 | 229.00 |
| 318.15 | 0.8003 | 249.00 |
| 318.15 | 0.8979 | 266.00 |
| 318.15 | 1.0000 | 286.00 |
| 323.15 | 0.0999 | 107.00 |
| 323.15 | 0.1999 | 131.00 |
| 323.15 | 0.2995 | 152.00 |
| 323.15 | 0.4000 | 172.00 |
| 323.15 | 0.5002 | 192.00 |
| 323.15 | 0.5997 | 211.00 |
| 323.15 | 0.7011 | 231.00 |
| 323.15 | 0.8003 | 250.00 |
| 323.15 | 0.8979 | 267.00 |
| 323.15 | 1.0000 | 287.00 |
| 328.15 | 0.0999 | 110.00 |
| 328.15 | 0.1999 | 134.00 |
| 328.15 | 0.2995 | 155.00 |
| 328.15 | 0.4000 | 175.00 |
| 328.15 | 0.5002 | 195.00 |
| 328.15 | 0.5997 | 214.00 |
| 328.15 | 0.7011 | 233.00 |
| 328.15 | 0.8003 | 252.00 |
| 328.15 | 0.8979 | 269.00 |
| 328.15 | 1.0000 | 289.00 |
| 333.15 | 0.0999 | 112.00 |
| 333.15 | 0.1999 | 137.00 |
| 333.15 | 0.2995 | 158.00 |
| 333.15 | 0.4000 | 178.00 |
| 333.15 | 0.5002 | 197.00 |
| 333.15 | 0.5997 | 216.00 |
| 333.15 | 0.7011 | 235.00 |
| 333.15 | 0.8003 | 254.00 |
| 333.15 | 0.8979 | 271.00 |
| 333.15 | 1.0000 | 290.00 |
| 338.15 | 0.0999 | 116.00 |
| 338.15 | 0.1999 | 141.00 |
| 338.15 | 0.2995 | 162.00 |
| 338.15 | 0.4000 | 181.00 |
| 338.15 | 0.5002 | 201.00 |
| 338.15 | 0.5997 | 219.00 |
| 338.15 | 0.7011 | 238.00 |
| 338.15 | 0.8003 | 257.00 |
| 338.15 | 0.8979 | 273.00 |
| 338.15 | 1.0000 | 292.00 |
| 343.15 | 0.0999 | 120.00 |
| 343.15 | 0.1999 | 146.00 |
| 343.15 | 0.2995 | 167.00 |
| 343.15 | 0.4000 | 185.00 |
| 343.15 | 0.5002 | 204.00 |
| 343.15 | 0.5997 | 223.00 |
| 343.15 | 0.7011 | 241.00 |
| 343.15 | 0.8003 | 260.00 |
| 343.15 | 0.8979 | 275.00 |
| 343.15 | 1.0000 | 293.00 |
| 348.15 | 0.0999 | 124.00 |
| 348.15 | 0.1999 | 152.00 |
| 348.15 | 0.2995 | 172.00 |
| 348.15 | 0.4000 | 189.00 |
| 348.15 | 0.5002 | 208.00 |
| 348.15 | 0.5997 | 227.00 |
| 348.15 | 0.7011 | 244.00 |
| 348.15 | 0.8003 | 262.00 |
| 348.15 | 0.8979 | 277.00 |
| 348.15 | 1.0000 | 295.00 |
| 353.15 | 0.0999 | 130.00 |
| 353.15 | 0.1999 | 158.00 |
| 353.15 | 0.2995 | 177.00 |
| 353.15 | 0.4000 | 194.00 |
| 353.15 | 0.5002 | 213.00 |
| 353.15 | 0.5997 | 231.00 |
| 353.15 | 0.7011 | 248.00 |
| 353.15 | 0.8003 | 265.00 |
| 353.15 | 0.8979 | 279.00 |
| 353.15 | 1.0000 | 296.00 |
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 303.15 | 0.0999 | 100.00 |
| 303.15 | 0.1999 | 121.00 |
| 303.15 | 0.2995 | 141.00 |
| 303.15 | 0.4000 | 161.00 |
| 303.15 | 0.5002 | 181.00 |
| 303.15 | 0.5997 | 201.00 |
| 303.15 | 0.7011 | 221.00 |
| 303.15 | 0.8003 | 240.00 |
| 303.15 | 0.8979 | 258.00 |
| 303.15 | 1.0000 | 279.00 |
| 308.15 | 0.0999 | 103.00 |
| 308.15 | 0.1999 | 125.00 |
| 308.15 | 0.2995 | 145.00 |
| 308.15 | 0.4000 | 165.00 |
| 308.15 | 0.5002 | 185.00 |
| 308.15 | 0.5997 | 205.00 |
| 308.15 | 0.7011 | 226.00 |
| 308.15 | 0.8003 | 245.00 |
| 308.15 | 0.8979 | 263.00 |
| 308.15 | 1.0000 | 284.00 |
| 313.15 | 0.0999 | 104.00 |
| 313.15 | 0.1999 | 127.00 |
| 313.15 | 0.2995 | 147.00 |
| 313.15 | 0.4000 | 167.00 |
| 313.15 | 0.5002 | 187.00 |
| 313.15 | 0.5997 | 207.00 |
| 313.15 | 0.7011 | 227.00 |
| 313.15 | 0.8003 | 247.00 |
| 313.15 | 0.8979 | 265.00 |
| 313.15 | 1.0000 | 285.00 |
| 318.15 | 0.0999 | 106.00 |
| 318.15 | 0.1999 | 129.00 |
| 318.15 | 0.2995 | 150.00 |
| 318.15 | 0.4000 | 170.00 |
| 318.15 | 0.5002 | 190.00 |
| 318.15 | 0.5997 | 209.00 |
| 318.15 | 0.7011 | 229.00 |
| 318.15 | 0.8003 | 249.00 |
| 318.15 | 0.8979 | 266.00 |
| 318.15 | 1.0000 | 286.00 |
| 323.15 | 0.0999 | 107.00 |
| 323.15 | 0.1999 | 131.00 |
| 323.15 | 0.2995 | 152.00 |
| 323.15 | 0.4000 | 172.00 |
| 323.15 | 0.5002 | 192.00 |
| 323.15 | 0.5997 | 211.00 |
| 323.15 | 0.7011 | 231.00 |
| 323.15 | 0.8003 | 250.00 |
| 323.15 | 0.8979 | 267.00 |
| 323.15 | 1.0000 | 287.00 |
| 328.15 | 0.0999 | 110.00 |
| 328.15 | 0.1999 | 134.00 |
| 328.15 | 0.2995 | 155.00 |
| 328.15 | 0.4000 | 175.00 |
| 328.15 | 0.5002 | 195.00 |
| 328.15 | 0.5997 | 214.00 |
| 328.15 | 0.7011 | 233.00 |
| 328.15 | 0.8003 | 252.00 |
| 328.15 | 0.8979 | 269.00 |
| 328.15 | 1.0000 | 289.00 |
| 333.15 | 0.0999 | 112.00 |
| 333.15 | 0.1999 | 137.00 |
| 333.15 | 0.2995 | 158.00 |
| 333.15 | 0.4000 | 178.00 |
| 333.15 | 0.5002 | 197.00 |
| 333.15 | 0.5997 | 216.00 |
| 333.15 | 0.7011 | 235.00 |
| 333.15 | 0.8003 | 254.00 |
| 333.15 | 0.8979 | 271.00 |
| 333.15 | 1.0000 | 290.00 |
| 338.15 | 0.0999 | 116.00 |
| 338.15 | 0.1999 | 141.00 |
| 338.15 | 0.2995 | 162.00 |
| 338.15 | 0.4000 | 181.00 |
| 338.15 | 0.5002 | 201.00 |
| 338.15 | 0.5997 | 219.00 |
| 338.15 | 0.7011 | 238.00 |
| 338.15 | 0.8003 | 257.00 |
| 338.15 | 0.8979 | 273.00 |
| 338.15 | 1.0000 | 292.00 |
| 343.15 | 0.0999 | 120.00 |
| 343.15 | 0.1999 | 146.00 |
| 343.15 | 0.2995 | 167.00 |
| 343.15 | 0.4000 | 185.00 |
| 343.15 | 0.5002 | 204.00 |
| 343.15 | 0.5997 | 223.00 |
| 343.15 | 0.7011 | 241.00 |
| 343.15 | 0.8003 | 260.00 |
| 343.15 | 0.8979 | 275.00 |
| 343.15 | 1.0000 | 293.00 |
| 348.15 | 0.0999 | 124.00 |
| 348.15 | 0.1999 | 152.00 |
| 348.15 | 0.2995 | 172.00 |
| 348.15 | 0.4000 | 189.00 |
| 348.15 | 0.5002 | 208.00 |
| 348.15 | 0.5997 | 227.00 |
| 348.15 | 0.7011 | 244.00 |
| 348.15 | 0.8003 | 262.00 |
| 348.15 | 0.8979 | 277.00 |
| 348.15 | 1.0000 | 295.00 |
| 353.15 | 0.0999 | 130.00 |
| 353.15 | 0.1999 | 158.00 |
| 353.15 | 0.2995 | 177.00 |
| 353.15 | 0.4000 | 194.00 |
| 353.15 | 0.5002 | 213.00 |
| 353.15 | 0.5997 | 231.00 |
| 353.15 | 0.7011 | 248.00 |
| 353.15 | 0.8003 | 265.00 |
| 353.15 | 0.8979 | 279.00 |
| 353.15 | 1.0000 | 296.00 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0500 | 0.0012 |
| 298.15 | 0.0500 | 0.0011 |
| 303.15 | 0.0500 | 0.0009 |
| 308.15 | 0.0500 | 0.0008 |
| 313.15 | 0.0500 | 0.0008 |
| 318.15 | 0.0500 | 0.0007 |
| 323.15 | 0.0500 | 0.0006 |
| 328.15 | 0.0500 | 0.0006 |
| 333.15 | 0.0500 | 0.0006 |
| 293.15 | 0.1000 | 0.0016 |
| 298.15 | 0.1000 | 0.0014 |
| 303.15 | 0.1000 | 0.0012 |
| 308.15 | 0.1000 | 0.0011 |
| 313.15 | 0.1000 | 0.0009 |
| 318.15 | 0.1000 | 0.0008 |
| 323.15 | 0.1000 | 0.0008 |
| 328.15 | 0.1000 | 0.0007 |
| 333.15 | 0.1000 | 0.0006 |
| 293.15 | 0.1500 | 0.0020 |
| 298.15 | 0.1500 | 0.0017 |
| 303.15 | 0.1500 | 0.0015 |
| 308.15 | 0.1500 | 0.0013 |
| 313.15 | 0.1500 | 0.0012 |
| 318.15 | 0.1500 | 0.0010 |
| 323.15 | 0.1500 | 0.0009 |
| 328.15 | 0.1500 | 0.0008 |
| 333.15 | 0.1500 | 0.0007 |
| 293.15 | 0.2000 | 0.0026 |
| 298.15 | 0.2000 | 0.0022 |
| 303.15 | 0.2000 | 0.0019 |
| 308.15 | 0.2000 | 0.0016 |
| 313.15 | 0.2000 | 0.0014 |
| 318.15 | 0.2000 | 0.0012 |
| 323.15 | 0.2000 | 0.0011 |
| 328.15 | 0.2000 | 0.0009 |
| 333.15 | 0.2000 | 0.0009 |
| 293.15 | 0.2500 | 0.0035 |
| 298.15 | 0.2500 | 0.0030 |
| 303.15 | 0.2500 | 0.0024 |
| 308.15 | 0.2500 | 0.0021 |
| 313.15 | 0.2500 | 0.0018 |
| 318.15 | 0.2500 | 0.0015 |
| 323.15 | 0.2500 | 0.0013 |
| 328.15 | 0.2500 | 0.0011 |
| 333.15 | 0.2500 | 0.0010 |
| 293.15 | 0.3000 | 0.0047 |
| 298.15 | 0.3000 | 0.0040 |
| 303.15 | 0.3000 | 0.0033 |
| 308.15 | 0.3000 | 0.0026 |
| 313.15 | 0.3000 | 0.0022 |
| 318.15 | 0.3000 | 0.0019 |
| 323.15 | 0.3000 | 0.0016 |
| 328.15 | 0.3000 | 0.0014 |
| 333.15 | 0.3000 | 0.0012 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0009 |
| 298.15 | 0.0500 | 0.0024 |
| 298.15 | 0.0700 | 0.0039 |
| 298.15 | 0.0999 | 0.0068 |
| 298.15 | 0.1992 | 0.0300 |
| 298.15 | 0.3000 | 0.0709 |
| 298.15 | 0.3997 | 0.1040 |
| 298.15 | 0.4991 | 0.1210 |
| 298.15 | 0.5990 | 0.1240 |
| 298.15 | 0.6991 | 0.1210 |
| 298.15 | 0.7997 | 0.1160 |
| 298.15 | 0.9002 | 0.1090 |
| 298.15 | 1.0000 | 0.0986 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.0500 | 0.0022 |
| 303.15 | 0.0700 | 0.0032 |
| 303.15 | 0.0999 | 0.0055 |
| 303.15 | 0.1992 | 0.0226 |
| 303.15 | 0.3000 | 0.0504 |
| 303.15 | 0.3997 | 0.0728 |
| 303.15 | 0.4991 | 0.0839 |
| 303.15 | 0.5990 | 0.0870 |
| 303.15 | 0.6991 | 0.0848 |
| 303.15 | 0.7997 | 0.0825 |
| 303.15 | 0.9002 | 0.0781 |
| 303.15 | 1.0000 | 0.0705 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.0500 | 0.0016 |
| 313.15 | 0.0700 | 0.0023 |
| 313.15 | 0.0999 | 0.0038 |
| 313.15 | 0.1992 | 0.0135 |
| 313.15 | 0.3000 | 0.0278 |
| 313.15 | 0.3997 | 0.0389 |
| 313.15 | 0.4991 | 0.0448 |
| 313.15 | 0.5990 | 0.0465 |
| 313.15 | 0.6991 | 0.0457 |
| 313.15 | 0.7997 | 0.0448 |
| 313.15 | 0.9002 | 0.0444 |
| 313.15 | 1.0000 | 0.0394 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.0500 | 0.0013 |
| 323.15 | 0.0700 | 0.0018 |
| 323.15 | 0.0999 | 0.0028 |
| 323.15 | 0.1992 | 0.0087 |
| 323.15 | 0.3000 | 0.0165 |
| 323.15 | 0.3997 | 0.0225 |
| 323.15 | 0.4991 | 0.0256 |
| 323.15 | 0.5990 | 0.0267 |
| 323.15 | 0.6991 | 0.0264 |
| 323.15 | 0.7997 | 0.0260 |
| 323.15 | 0.9002 | 0.0260 |
| 323.15 | 1.0000 | 0.0234 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.0500 | 0.0010 |
| 333.15 | 0.0700 | 0.0014 |
| 333.15 | 0.0999 | 0.0021 |
| 333.15 | 0.1992 | 0.0059 |
| 333.15 | 0.3000 | 0.0105 |
| 333.15 | 0.3997 | 0.0138 |
| 333.15 | 0.4991 | 0.0158 |
| 333.15 | 0.5990 | 0.0165 |
| 333.15 | 0.6991 | 0.0165 |
| 333.15 | 0.7997 | 0.0164 |
| 333.15 | 0.9002 | 0.0165 |
| 333.15 | 1.0000 | 0.0148 |
| 343.15 | 0.0000 | 0.0004 |
| 343.15 | 0.0500 | 0.0008 |
| 343.15 | 0.0700 | 0.0011 |
| 343.15 | 0.0999 | 0.0016 |
| 343.15 | 0.1992 | 0.0042 |
| 343.15 | 0.3000 | 0.0070 |
| 343.15 | 0.3997 | 0.0091 |
| 343.15 | 0.4991 | 0.0103 |
| 343.15 | 0.5990 | 0.0108 |
| 343.15 | 0.6991 | 0.0108 |
| 343.15 | 0.7997 | 0.0108 |
| 343.15 | 0.9002 | 0.0107 |
| 343.15 | 1.0000 | 0.0101 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0500 | 0.0012 |
| 298.15 | 0.0500 | 0.0011 |
| 303.15 | 0.0500 | 0.0009 |
| 308.15 | 0.0500 | 0.0008 |
| 313.15 | 0.0500 | 0.0008 |
| 318.15 | 0.0500 | 0.0007 |
| 323.15 | 0.0500 | 0.0006 |
| 328.15 | 0.0500 | 0.0006 |
| 333.15 | 0.0500 | 0.0006 |
| 293.15 | 0.1000 | 0.0016 |
| 298.15 | 0.1000 | 0.0014 |
| 303.15 | 0.1000 | 0.0012 |
| 308.15 | 0.1000 | 0.0011 |
| 313.15 | 0.1000 | 0.0009 |
| 318.15 | 0.1000 | 0.0008 |
| 323.15 | 0.1000 | 0.0008 |
| 328.15 | 0.1000 | 0.0007 |
| 333.15 | 0.1000 | 0.0006 |
| 293.15 | 0.1500 | 0.0020 |
| 298.15 | 0.1500 | 0.0017 |
| 303.15 | 0.1500 | 0.0015 |
| 308.15 | 0.1500 | 0.0013 |
| 313.15 | 0.1500 | 0.0012 |
| 318.15 | 0.1500 | 0.0010 |
| 323.15 | 0.1500 | 0.0009 |
| 328.15 | 0.1500 | 0.0008 |
| 333.15 | 0.1500 | 0.0007 |
| 293.15 | 0.2000 | 0.0026 |
| 298.15 | 0.2000 | 0.0022 |
| 303.15 | 0.2000 | 0.0019 |
| 308.15 | 0.2000 | 0.0016 |
| 313.15 | 0.2000 | 0.0014 |
| 318.15 | 0.2000 | 0.0012 |
| 323.15 | 0.2000 | 0.0011 |
| 328.15 | 0.2000 | 0.0009 |
| 333.15 | 0.2000 | 0.0009 |
| 293.15 | 0.2500 | 0.0035 |
| 298.15 | 0.2500 | 0.0030 |
| 303.15 | 0.2500 | 0.0024 |
| 308.15 | 0.2500 | 0.0021 |
| 313.15 | 0.2500 | 0.0018 |
| 318.15 | 0.2500 | 0.0015 |
| 323.15 | 0.2500 | 0.0013 |
| 328.15 | 0.2500 | 0.0011 |
| 333.15 | 0.2500 | 0.0010 |
| 293.15 | 0.3000 | 0.0047 |
| 298.15 | 0.3000 | 0.0040 |
| 303.15 | 0.3000 | 0.0033 |
| 308.15 | 0.3000 | 0.0026 |
| 313.15 | 0.3000 | 0.0022 |
| 318.15 | 0.3000 | 0.0019 |
| 323.15 | 0.3000 | 0.0016 |
| 328.15 | 0.3000 | 0.0014 |
| 333.15 | 0.3000 | 0.0012 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0009 |
| 298.15 | 0.0500 | 0.0024 |
| 298.15 | 0.0700 | 0.0039 |
| 298.15 | 0.0999 | 0.0068 |
| 298.15 | 0.1992 | 0.0300 |
| 298.15 | 0.3000 | 0.0709 |
| 298.15 | 0.3997 | 0.1040 |
| 298.15 | 0.4991 | 0.1210 |
| 298.15 | 0.5990 | 0.1240 |
| 298.15 | 0.6991 | 0.1210 |
| 298.15 | 0.7997 | 0.1160 |
| 298.15 | 0.9002 | 0.1090 |
| 298.15 | 1.0000 | 0.0986 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.0500 | 0.0022 |
| 303.15 | 0.0700 | 0.0032 |
| 303.15 | 0.0999 | 0.0055 |
| 303.15 | 0.1992 | 0.0226 |
| 303.15 | 0.3000 | 0.0504 |
| 303.15 | 0.3997 | 0.0728 |
| 303.15 | 0.4991 | 0.0839 |
| 303.15 | 0.5990 | 0.0870 |
| 303.15 | 0.6991 | 0.0848 |
| 303.15 | 0.7997 | 0.0825 |
| 303.15 | 0.9002 | 0.0781 |
| 303.15 | 1.0000 | 0.0705 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.0500 | 0.0016 |
| 313.15 | 0.0700 | 0.0023 |
| 313.15 | 0.0999 | 0.0038 |
| 313.15 | 0.1992 | 0.0135 |
| 313.15 | 0.3000 | 0.0278 |
| 313.15 | 0.3997 | 0.0389 |
| 313.15 | 0.4991 | 0.0448 |
| 313.15 | 0.5990 | 0.0465 |
| 313.15 | 0.6991 | 0.0457 |
| 313.15 | 0.7997 | 0.0448 |
| 313.15 | 0.9002 | 0.0444 |
| 313.15 | 1.0000 | 0.0394 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.0500 | 0.0013 |
| 323.15 | 0.0700 | 0.0018 |
| 323.15 | 0.0999 | 0.0028 |
| 323.15 | 0.1992 | 0.0087 |
| 323.15 | 0.3000 | 0.0165 |
| 323.15 | 0.3997 | 0.0225 |
| 323.15 | 0.4991 | 0.0256 |
| 323.15 | 0.5990 | 0.0267 |
| 323.15 | 0.6991 | 0.0264 |
| 323.15 | 0.7997 | 0.0260 |
| 323.15 | 0.9002 | 0.0260 |
| 323.15 | 1.0000 | 0.0234 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.0500 | 0.0010 |
| 333.15 | 0.0700 | 0.0014 |
| 333.15 | 0.0999 | 0.0021 |
| 333.15 | 0.1992 | 0.0059 |
| 333.15 | 0.3000 | 0.0105 |
| 333.15 | 0.3997 | 0.0138 |
| 333.15 | 0.4991 | 0.0158 |
| 333.15 | 0.5990 | 0.0165 |
| 333.15 | 0.6991 | 0.0165 |
| 333.15 | 0.7997 | 0.0164 |
| 333.15 | 0.9002 | 0.0165 |
| 333.15 | 1.0000 | 0.0148 |
| 343.15 | 0.0000 | 0.0004 |
| 343.15 | 0.0500 | 0.0008 |
| 343.15 | 0.0700 | 0.0011 |
| 343.15 | 0.0999 | 0.0016 |
| 343.15 | 0.1992 | 0.0042 |
| 343.15 | 0.3000 | 0.0070 |
| 343.15 | 0.3997 | 0.0091 |
| 343.15 | 0.4991 | 0.0103 |
| 343.15 | 0.5990 | 0.0108 |
| 343.15 | 0.6991 | 0.0108 |
| 343.15 | 0.7997 | 0.0108 |
| 343.15 | 0.9002 | 0.0107 |
| 343.15 | 1.0000 | 0.0101 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 0.0298 | -0.7710 |
| 298.15 | 0.0496 | -1.273 |
| 298.15 | 0.0699 | -1.713 |
| 298.15 | 0.0992 | -2.241 |
| 298.15 | 0.1503 | -3.0 |
| 298.15 | 0.2015 | -3.447 |
| 298.15 | 0.2962 | -3.909 |
| 298.15 | 0.2982 | -3.918 |
| 298.15 | 0.3484 | -4.009 |
| 298.15 | 0.3994 | -3.955 |
| 298.15 | 0.4454 | -3.771 |
| 298.15 | 0.4962 | -3.489 |
| 298.15 | 0.5050 | -3.433 |
| 298.15 | 0.5922 | -2.865 |
| 298.15 | 0.6969 | -2.192 |
| 298.15 | 0.7700 | -1.711 |
| 298.15 | 0.9077 | -0.7790 |
| 313.15 | 0.0299 | -0.9360 |
| 313.15 | 0.0498 | -1.317 |
| 313.15 | 0.0701 | -1.72 |
| 313.15 | 0.1000 | -2.338 |
| 313.15 | 0.1495 | -3.051 |
| 313.15 | 0.2002 | -3.62 |
| 313.15 | 0.2956 | -4.119 |
| 313.15 | 0.3547 | -4.234 |
| 313.15 | 0.4001 | -4.15 |
| 313.15 | 0.4461 | -3.976 |
| 313.15 | 0.4893 | -3.784 |
| 313.15 | 0.6009 | -3.148 |
| 313.15 | 0.6723 | -2.669 |
| 313.15 | 0.7961 | -1.714 |
| 313.15 | 0.9041 | -0.8880 |
| 323.15 | 0.0301 | -0.6170 |
| 323.15 | 0.0498 | -1.029 |
| 323.15 | 0.0697 | -1.594 |
| 323.15 | 0.0992 | -2.037 |
| 323.15 | 0.1491 | -2.915 |
| 323.15 | 0.1988 | -3.414 |
| 323.15 | 0.3014 | -3.815 |
| 323.15 | 0.3527 | -3.938 |
| 323.15 | 0.3958 | -3.916 |
| 323.15 | 0.4971 | -3.6 |
| 323.15 | 0.5908 | -3.027 |
| 323.15 | 0.7056 | -2.241 |
| 323.15 | 0.7484 | -1.939 |
| 323.15 | 0.8999 | -0.8200 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1031 | -2.316 |
| 0.2020 | -3.609 |
| 0.3019 | -4.028 |
| 0.3567 | -4.163 |
| 0.4023 | -4.006 |
| 0.4991 | -3.681 |
| 0.5997 | -3.096 |
| 0.7027 | -2.421 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 0.0298 | -0.7710 |
| 298.15 | 0.0496 | -1.273 |
| 298.15 | 0.0699 | -1.713 |
| 298.15 | 0.0992 | -2.241 |
| 298.15 | 0.1503 | -3.0 |
| 298.15 | 0.2015 | -3.447 |
| 298.15 | 0.2962 | -3.909 |
| 298.15 | 0.2982 | -3.918 |
| 298.15 | 0.3484 | -4.009 |
| 298.15 | 0.3994 | -3.955 |
| 298.15 | 0.4454 | -3.771 |
| 298.15 | 0.4962 | -3.489 |
| 298.15 | 0.5050 | -3.433 |
| 298.15 | 0.5922 | -2.865 |
| 298.15 | 0.6969 | -2.192 |
| 298.15 | 0.7700 | -1.711 |
| 298.15 | 0.9077 | -0.7790 |
| 313.15 | 0.0299 | -0.9360 |
| 313.15 | 0.0498 | -1.317 |
| 313.15 | 0.0701 | -1.72 |
| 313.15 | 0.1000 | -2.338 |
| 313.15 | 0.1495 | -3.051 |
| 313.15 | 0.2002 | -3.62 |
| 313.15 | 0.2956 | -4.119 |
| 313.15 | 0.3547 | -4.234 |
| 313.15 | 0.4001 | -4.15 |
| 313.15 | 0.4461 | -3.976 |
| 313.15 | 0.4893 | -3.784 |
| 313.15 | 0.6009 | -3.148 |
| 313.15 | 0.6723 | -2.669 |
| 313.15 | 0.7961 | -1.714 |
| 313.15 | 0.9041 | -0.8880 |
| 323.15 | 0.0301 | -0.6170 |
| 323.15 | 0.0498 | -1.029 |
| 323.15 | 0.0697 | -1.594 |
| 323.15 | 0.0992 | -2.037 |
| 323.15 | 0.1491 | -2.915 |
| 323.15 | 0.1988 | -3.414 |
| 323.15 | 0.3014 | -3.815 |
| 323.15 | 0.3527 | -3.938 |
| 323.15 | 0.3958 | -3.916 |
| 323.15 | 0.4971 | -3.6 |
| 323.15 | 0.5908 | -3.027 |
| 323.15 | 0.7056 | -2.241 |
| 323.15 | 0.7484 | -1.939 |
| 323.15 | 0.8999 | -0.8200 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1031 | -2.316 |
| 0.2020 | -3.609 |
| 0.3019 | -4.028 |
| 0.3567 | -4.163 |
| 0.4023 | -4.006 |
| 0.4991 | -3.681 |
| 0.5997 | -3.096 |
| 0.7027 | -2.421 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 0.1000 | 313.20 | 7.00 |
| 0.1000 | 328.20 | 15.00 |
| 0.1000 | 343.20 | 28.70 |
| 0.1000 | 358.20 | 51.80 |
| 0.3000 | 358.20 | 46.20 |
Vapor or sublimation pressure, kPa [ref]
| Fixed | Measured | |
|---|---|---|
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
| 0.1000 | 313.20 | 7.00 |
| 0.1000 | 328.20 | 15.00 |
| 0.1000 | 343.20 | 28.70 |
| 0.1000 | 358.20 | 51.80 |
| 0.3000 | 358.20 | 46.20 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0500 | 1.3406 |
| 298.15 | 0.0500 | 1.3401 |
| 303.15 | 0.0500 | 1.3394 |
| 308.15 | 0.0500 | 1.3387 |
| 313.15 | 0.0500 | 1.3378 |
| 318.15 | 0.0500 | 1.3368 |
| 323.15 | 0.0500 | 1.3358 |
| 328.15 | 0.0500 | 1.3347 |
| 333.15 | 0.0500 | 1.3335 |
| 293.15 | 0.1000 | 1.3452 |
| 298.15 | 0.1000 | 1.3446 |
| 303.15 | 0.1000 | 1.3438 |
| 308.15 | 0.1000 | 1.343 |
| 313.15 | 0.1000 | 1.3421 |
| 318.15 | 0.1000 | 1.341 |
| 323.15 | 0.1000 | 1.3398 |
| 328.15 | 0.1000 | 1.3385 |
| 333.15 | 0.1000 | 1.3371 |
| 293.15 | 0.1500 | 1.351 |
| 298.15 | 0.1500 | 1.3504 |
| 303.15 | 0.1500 | 1.3496 |
| 308.15 | 0.1500 | 1.3487 |
| 313.15 | 0.1500 | 1.3476 |
| 318.15 | 0.1500 | 1.3464 |
| 323.15 | 0.1500 | 1.3451 |
| 328.15 | 0.1500 | 1.3436 |
| 333.15 | 0.1500 | 1.342 |
| 293.15 | 0.2000 | 1.3582 |
| 298.15 | 0.2000 | 1.3575 |
| 303.15 | 0.2000 | 1.3567 |
| 308.15 | 0.2000 | 1.3558 |
| 313.15 | 0.2000 | 1.3548 |
| 318.15 | 0.2000 | 1.3536 |
| 323.15 | 0.2000 | 1.3523 |
| 328.15 | 0.2000 | 1.3508 |
| 333.15 | 0.2000 | 1.3491 |
| 293.15 | 0.2500 | 1.366 |
| 298.15 | 0.2500 | 1.3652 |
| 303.15 | 0.2500 | 1.3643 |
| 308.15 | 0.2500 | 1.3633 |
| 313.15 | 0.2500 | 1.3622 |
| 318.15 | 0.2500 | 1.361 |
| 323.15 | 0.2500 | 1.3597 |
| 328.15 | 0.2500 | 1.3582 |
| 333.15 | 0.2500 | 1.3566 |
| 293.15 | 0.3000 | 1.3752 |
| 298.15 | 0.3000 | 1.3744 |
| 303.15 | 0.3000 | 1.3735 |
| 308.15 | 0.3000 | 1.3724 |
| 313.15 | 0.3000 | 1.3712 |
| 318.15 | 0.3000 | 1.3698 |
| 323.15 | 0.3000 | 1.3682 |
| 328.15 | 0.3000 | 1.3664 |
| 333.15 | 0.3000 | 1.3648 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.3326 |
| 298.15 | 0.0500 | 1.3701 |
| 298.15 | 0.0700 | 1.382 |
| 298.15 | 0.1000 | 1.398 |
| 298.15 | 0.2000 | 1.4331 |
| 298.15 | 0.3000 | 1.4525 |
| 298.15 | 0.4000 | 1.4632 |
| 298.15 | 0.5000 | 1.4703 |
| 298.15 | 0.5996 | 1.475 |
| 298.15 | 0.7011 | 1.4785 |
| 298.15 | 0.8002 | 1.481 |
| 298.15 | 0.8979 | 1.4829 |
| 298.15 | 1.0000 | 1.4845 |
| 303.15 | 0.0000 | 1.332 |
| 303.15 | 0.0500 | 1.3693 |
| 303.15 | 0.0700 | 1.3811 |
| 303.15 | 0.1000 | 1.3968 |
| 303.15 | 0.2000 | 1.4318 |
| 303.15 | 0.3000 | 1.4509 |
| 303.15 | 0.4000 | 1.4616 |
| 303.15 | 0.5000 | 1.4686 |
| 303.15 | 0.5996 | 1.4732 |
| 303.15 | 0.7011 | 1.4767 |
| 303.15 | 0.8002 | 1.4792 |
| 303.15 | 0.8979 | 1.481 |
| 303.15 | 1.0000 | 1.4827 |
| 313.15 | 0.0000 | 1.3307 |
| 313.15 | 0.0500 | 1.3675 |
| 313.15 | 0.0700 | 1.3791 |
| 313.15 | 0.1000 | 1.3945 |
| 313.15 | 0.2000 | 1.4289 |
| 313.15 | 0.3000 | 1.4476 |
| 313.15 | 0.4000 | 1.4581 |
| 313.15 | 0.5000 | 1.465 |
| 313.15 | 0.5996 | 1.4696 |
| 313.15 | 0.7011 | 1.4731 |
| 313.15 | 0.8002 | 1.4755 |
| 313.15 | 0.8979 | 1.4773 |
| 313.15 | 1.0000 | 1.4788 |
| 323.15 | 0.0000 | 1.3291 |
| 323.15 | 0.0500 | 1.3654 |
| 323.15 | 0.0700 | 1.377 |
| 323.15 | 0.1000 | 1.3921 |
| 323.15 | 0.2000 | 1.4258 |
| 323.15 | 0.3000 | 1.4443 |
| 323.15 | 0.4000 | 1.4546 |
| 323.15 | 0.5000 | 1.4615 |
| 323.15 | 0.5996 | 1.466 |
| 323.15 | 0.7011 | 1.4694 |
| 323.15 | 0.8002 | 1.4718 |
| 323.15 | 0.8979 | 1.4736 |
| 323.15 | 1.0000 | 1.4752 |
| 333.15 | 0.0000 | 1.3273 |
| 333.15 | 0.0500 | 1.3637 |
| 333.15 | 0.0700 | 1.3751 |
| 333.15 | 0.1000 | 1.3899 |
| 333.15 | 0.2000 | 1.4226 |
| 333.15 | 0.3000 | 1.4409 |
| 333.15 | 0.4000 | 1.4511 |
| 333.15 | 0.5000 | 1.4578 |
| 333.15 | 0.5996 | 1.4622 |
| 333.15 | 0.7011 | 1.4656 |
| 333.15 | 0.8002 | 1.4681 |
| 333.15 | 0.8979 | 1.4698 |
| 333.15 | 1.0000 | 1.4713 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 293.15 | 0.0500 | 1.3406 |
| 298.15 | 0.0500 | 1.3401 |
| 303.15 | 0.0500 | 1.3394 |
| 308.15 | 0.0500 | 1.3387 |
| 313.15 | 0.0500 | 1.3378 |
| 318.15 | 0.0500 | 1.3368 |
| 323.15 | 0.0500 | 1.3358 |
| 328.15 | 0.0500 | 1.3347 |
| 333.15 | 0.0500 | 1.3335 |
| 293.15 | 0.1000 | 1.3452 |
| 298.15 | 0.1000 | 1.3446 |
| 303.15 | 0.1000 | 1.3438 |
| 308.15 | 0.1000 | 1.343 |
| 313.15 | 0.1000 | 1.3421 |
| 318.15 | 0.1000 | 1.341 |
| 323.15 | 0.1000 | 1.3398 |
| 328.15 | 0.1000 | 1.3385 |
| 333.15 | 0.1000 | 1.3371 |
| 293.15 | 0.1500 | 1.351 |
| 298.15 | 0.1500 | 1.3504 |
| 303.15 | 0.1500 | 1.3496 |
| 308.15 | 0.1500 | 1.3487 |
| 313.15 | 0.1500 | 1.3476 |
| 318.15 | 0.1500 | 1.3464 |
| 323.15 | 0.1500 | 1.3451 |
| 328.15 | 0.1500 | 1.3436 |
| 333.15 | 0.1500 | 1.342 |
| 293.15 | 0.2000 | 1.3582 |
| 298.15 | 0.2000 | 1.3575 |
| 303.15 | 0.2000 | 1.3567 |
| 308.15 | 0.2000 | 1.3558 |
| 313.15 | 0.2000 | 1.3548 |
| 318.15 | 0.2000 | 1.3536 |
| 323.15 | 0.2000 | 1.3523 |
| 328.15 | 0.2000 | 1.3508 |
| 333.15 | 0.2000 | 1.3491 |
| 293.15 | 0.2500 | 1.366 |
| 298.15 | 0.2500 | 1.3652 |
| 303.15 | 0.2500 | 1.3643 |
| 308.15 | 0.2500 | 1.3633 |
| 313.15 | 0.2500 | 1.3622 |
| 318.15 | 0.2500 | 1.361 |
| 323.15 | 0.2500 | 1.3597 |
| 328.15 | 0.2500 | 1.3582 |
| 333.15 | 0.2500 | 1.3566 |
| 293.15 | 0.3000 | 1.3752 |
| 298.15 | 0.3000 | 1.3744 |
| 303.15 | 0.3000 | 1.3735 |
| 308.15 | 0.3000 | 1.3724 |
| 313.15 | 0.3000 | 1.3712 |
| 318.15 | 0.3000 | 1.3698 |
| 323.15 | 0.3000 | 1.3682 |
| 328.15 | 0.3000 | 1.3664 |
| 333.15 | 0.3000 | 1.3648 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.3326 |
| 298.15 | 0.0500 | 1.3701 |
| 298.15 | 0.0700 | 1.382 |
| 298.15 | 0.1000 | 1.398 |
| 298.15 | 0.2000 | 1.4331 |
| 298.15 | 0.3000 | 1.4525 |
| 298.15 | 0.4000 | 1.4632 |
| 298.15 | 0.5000 | 1.4703 |
| 298.15 | 0.5996 | 1.475 |
| 298.15 | 0.7011 | 1.4785 |
| 298.15 | 0.8002 | 1.481 |
| 298.15 | 0.8979 | 1.4829 |
| 298.15 | 1.0000 | 1.4845 |
| 303.15 | 0.0000 | 1.332 |
| 303.15 | 0.0500 | 1.3693 |
| 303.15 | 0.0700 | 1.3811 |
| 303.15 | 0.1000 | 1.3968 |
| 303.15 | 0.2000 | 1.4318 |
| 303.15 | 0.3000 | 1.4509 |
| 303.15 | 0.4000 | 1.4616 |
| 303.15 | 0.5000 | 1.4686 |
| 303.15 | 0.5996 | 1.4732 |
| 303.15 | 0.7011 | 1.4767 |
| 303.15 | 0.8002 | 1.4792 |
| 303.15 | 0.8979 | 1.481 |
| 303.15 | 1.0000 | 1.4827 |
| 313.15 | 0.0000 | 1.3307 |
| 313.15 | 0.0500 | 1.3675 |
| 313.15 | 0.0700 | 1.3791 |
| 313.15 | 0.1000 | 1.3945 |
| 313.15 | 0.2000 | 1.4289 |
| 313.15 | 0.3000 | 1.4476 |
| 313.15 | 0.4000 | 1.4581 |
| 313.15 | 0.5000 | 1.465 |
| 313.15 | 0.5996 | 1.4696 |
| 313.15 | 0.7011 | 1.4731 |
| 313.15 | 0.8002 | 1.4755 |
| 313.15 | 0.8979 | 1.4773 |
| 313.15 | 1.0000 | 1.4788 |
| 323.15 | 0.0000 | 1.3291 |
| 323.15 | 0.0500 | 1.3654 |
| 323.15 | 0.0700 | 1.377 |
| 323.15 | 0.1000 | 1.3921 |
| 323.15 | 0.2000 | 1.4258 |
| 323.15 | 0.3000 | 1.4443 |
| 323.15 | 0.4000 | 1.4546 |
| 323.15 | 0.5000 | 1.4615 |
| 323.15 | 0.5996 | 1.466 |
| 323.15 | 0.7011 | 1.4694 |
| 323.15 | 0.8002 | 1.4718 |
| 323.15 | 0.8979 | 1.4736 |
| 323.15 | 1.0000 | 1.4752 |
| 333.15 | 0.0000 | 1.3273 |
| 333.15 | 0.0500 | 1.3637 |
| 333.15 | 0.0700 | 1.3751 |
| 333.15 | 0.1000 | 1.3899 |
| 333.15 | 0.2000 | 1.4226 |
| 333.15 | 0.3000 | 1.4409 |
| 333.15 | 0.4000 | 1.4511 |
| 333.15 | 0.5000 | 1.4578 |
| 333.15 | 0.5996 | 1.4622 |
| 333.15 | 0.7011 | 1.4656 |
| 333.15 | 0.8002 | 1.4681 |
| 333.15 | 0.8979 | 1.4698 |
| 333.15 | 1.0000 | 1.4713 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 997.04 |
| 298.15 | 0.0500 | 1015.65 |
| 298.15 | 0.0700 | 1022.28 |
| 298.15 | 0.0999 | 1030.85 |
| 298.15 | 0.1992 | 1047.37 |
| 298.15 | 0.3000 | 1050.66 |
| 298.15 | 0.3997 | 1048.18 |
| 298.15 | 0.4991 | 1044.05 |
| 298.15 | 0.5990 | 1039.62 |
| 298.15 | 0.6991 | 1035.48 |
| 298.15 | 0.7997 | 1031.83 |
| 298.15 | 0.9002 | 1028.28 |
| 298.15 | 1.0000 | 1025.28 |
| 303.15 | 0.0000 | 995.64 |
| 303.15 | 0.0500 | 1013.65 |
| 303.15 | 0.0700 | 1020.01 |
| 303.15 | 0.0999 | 1028.24 |
| 303.15 | 0.1992 | 1044.02 |
| 303.15 | 0.3000 | 1047.05 |
| 303.15 | 0.3997 | 1044.5 |
| 303.15 | 0.4991 | 1040.33 |
| 303.15 | 0.5990 | 1035.89 |
| 303.15 | 0.6991 | 1031.74 |
| 303.15 | 0.7997 | 1028.11 |
| 303.15 | 0.9002 | 1024.57 |
| 303.15 | 1.0000 | 1021.53 |
| 313.15 | 0.0000 | 992.21 |
| 313.15 | 0.0500 | 1009.22 |
| 313.15 | 0.0700 | 1015.13 |
| 313.15 | 0.0999 | 1022.7 |
| 313.15 | 0.1992 | 1037.13 |
| 313.15 | 0.3000 | 1039.7 |
| 313.15 | 0.3997 | 1037.01 |
| 313.15 | 0.4991 | 1032.79 |
| 313.15 | 0.5990 | 1028.36 |
| 313.15 | 0.6991 | 1024.21 |
| 313.15 | 0.7997 | 1020.57 |
| 313.15 | 0.9002 | 1017.06 |
| 313.15 | 1.0000 | 1014.02 |
| 323.15 | 0.0000 | 988.03 |
| 323.15 | 0.0500 | 1004.24 |
| 323.15 | 0.0700 | 1009.76 |
| 323.15 | 0.0999 | 1016.8 |
| 323.15 | 0.1992 | 1030.03 |
| 323.15 | 0.3000 | 1032.15 |
| 323.15 | 0.3997 | 1029.37 |
| 323.15 | 0.4991 | 1025.13 |
| 323.15 | 0.5990 | 1020.71 |
| 323.15 | 0.6991 | 1016.59 |
| 323.15 | 0.7997 | 1012.96 |
| 323.15 | 0.9002 | 1009.48 |
| 323.15 | 1.0000 | 1006.44 |
| 333.15 | 0.0000 | 983.19 |
| 333.15 | 0.0500 | 998.75 |
| 333.15 | 0.0700 | 1003.89 |
| 333.15 | 0.0999 | 1010.53 |
| 333.15 | 0.1992 | 1022.69 |
| 333.15 | 0.3000 | 1024.44 |
| 333.15 | 0.3997 | 1021.57 |
| 333.15 | 0.4991 | 1017.35 |
| 333.15 | 0.5990 | 1012.96 |
| 333.15 | 0.6991 | 1008.88 |
| 333.15 | 0.7997 | 1005.3 |
| 333.15 | 0.9002 | 1001.84 |
| 333.15 | 1.0000 | 998.83 |
| 343.15 | 0.0000 | 977.75 |
| 343.15 | 0.0500 | 992.77 |
| 343.15 | 0.0700 | 997.34 |
| 343.15 | 0.0999 | 1003.89 |
| 343.15 | 0.1992 | 1015.09 |
| 343.15 | 0.3000 | 1016.53 |
| 343.15 | 0.3997 | 1013.6 |
| 343.15 | 0.4991 | 1009.42 |
| 343.15 | 0.5990 | 1005.1 |
| 343.15 | 0.6991 | 1001.06 |
| 343.15 | 0.7997 | 997.54 |
| 343.15 | 0.9002 | 994.11 |
| 343.15 | 1.0000 | 991.15 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 997.04 |
| 298.15 | 0.0500 | 1015.65 |
| 298.15 | 0.0700 | 1022.28 |
| 298.15 | 0.0999 | 1030.85 |
| 298.15 | 0.1992 | 1047.37 |
| 298.15 | 0.3000 | 1050.66 |
| 298.15 | 0.3997 | 1048.18 |
| 298.15 | 0.4991 | 1044.05 |
| 298.15 | 0.5990 | 1039.62 |
| 298.15 | 0.6991 | 1035.48 |
| 298.15 | 0.7997 | 1031.83 |
| 298.15 | 0.9002 | 1028.28 |
| 298.15 | 1.0000 | 1025.28 |
| 303.15 | 0.0000 | 995.64 |
| 303.15 | 0.0500 | 1013.65 |
| 303.15 | 0.0700 | 1020.01 |
| 303.15 | 0.0999 | 1028.24 |
| 303.15 | 0.1992 | 1044.02 |
| 303.15 | 0.3000 | 1047.05 |
| 303.15 | 0.3997 | 1044.5 |
| 303.15 | 0.4991 | 1040.33 |
| 303.15 | 0.5990 | 1035.89 |
| 303.15 | 0.6991 | 1031.74 |
| 303.15 | 0.7997 | 1028.11 |
| 303.15 | 0.9002 | 1024.57 |
| 303.15 | 1.0000 | 1021.53 |
| 313.15 | 0.0000 | 992.21 |
| 313.15 | 0.0500 | 1009.22 |
| 313.15 | 0.0700 | 1015.13 |
| 313.15 | 0.0999 | 1022.7 |
| 313.15 | 0.1992 | 1037.13 |
| 313.15 | 0.3000 | 1039.7 |
| 313.15 | 0.3997 | 1037.01 |
| 313.15 | 0.4991 | 1032.79 |
| 313.15 | 0.5990 | 1028.36 |
| 313.15 | 0.6991 | 1024.21 |
| 313.15 | 0.7997 | 1020.57 |
| 313.15 | 0.9002 | 1017.06 |
| 313.15 | 1.0000 | 1014.02 |
| 323.15 | 0.0000 | 988.03 |
| 323.15 | 0.0500 | 1004.24 |
| 323.15 | 0.0700 | 1009.76 |
| 323.15 | 0.0999 | 1016.8 |
| 323.15 | 0.1992 | 1030.03 |
| 323.15 | 0.3000 | 1032.15 |
| 323.15 | 0.3997 | 1029.37 |
| 323.15 | 0.4991 | 1025.13 |
| 323.15 | 0.5990 | 1020.71 |
| 323.15 | 0.6991 | 1016.59 |
| 323.15 | 0.7997 | 1012.96 |
| 323.15 | 0.9002 | 1009.48 |
| 323.15 | 1.0000 | 1006.44 |
| 333.15 | 0.0000 | 983.19 |
| 333.15 | 0.0500 | 998.75 |
| 333.15 | 0.0700 | 1003.89 |
| 333.15 | 0.0999 | 1010.53 |
| 333.15 | 0.1992 | 1022.69 |
| 333.15 | 0.3000 | 1024.44 |
| 333.15 | 0.3997 | 1021.57 |
| 333.15 | 0.4991 | 1017.35 |
| 333.15 | 0.5990 | 1012.96 |
| 333.15 | 0.6991 | 1008.88 |
| 333.15 | 0.7997 | 1005.3 |
| 333.15 | 0.9002 | 1001.84 |
| 333.15 | 1.0000 | 998.83 |
| 343.15 | 0.0000 | 977.75 |
| 343.15 | 0.0500 | 992.77 |
| 343.15 | 0.0700 | 997.34 |
| 343.15 | 0.0999 | 1003.89 |
| 343.15 | 0.1992 | 1015.09 |
| 343.15 | 0.3000 | 1016.53 |
| 343.15 | 0.3997 | 1013.6 |
| 343.15 | 0.4991 | 1009.42 |
| 343.15 | 0.5990 | 1005.1 |
| 343.15 | 0.6991 | 1001.06 |
| 343.15 | 0.7997 | 997.54 |
| 343.15 | 0.9002 | 994.11 |
| 343.15 | 1.0000 | 991.15 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 86.66 (Liquid)
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0580 | 369.65 |
| 0.1010 | 369.80 |
| 0.1500 | 370.61 |
| 0.2440 | 371.06 |
| 0.3530 | 372.49 |
| 0.4340 | 373.50 |
| 0.4830 | 374.87 |
| 0.5380 | 375.86 |
| 0.5740 | 376.86 |
| 0.6070 | 378.06 |
| 0.6590 | 380.81 |
| 0.7050 | 382.26 |
| 0.6900 | 381.56 |
| 0.8860 | 407.73 |
| 0.8840 | 412.22 |
| 0.9700 | 468.15 |
| 0.9800 | 515.15 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 86.66 (Liquid)
| Mass fraction of Ethanol, 2-[(2-aminoethyl)amino]- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0580 | 369.65 |
| 0.1010 | 369.80 |
| 0.1500 | 370.61 |
| 0.2440 | 371.06 |
| 0.3530 | 372.49 |
| 0.4340 | 373.50 |
| 0.4830 | 374.87 |
| 0.5380 | 375.86 |
| 0.5740 | 376.86 |
| 0.6070 | 378.06 |
| 0.6590 | 380.81 |
| 0.7050 | 382.26 |
| 0.6900 | 381.56 |
| 0.8860 | 407.73 |
| 0.8840 | 412.22 |
| 0.9700 | 468.15 |
| 0.9800 | 515.15 |
Sources
- Molar excess enthalpy (HEm) for various {alkanolamine (1) + water (2)} systems at T = (298.15, 313.15, and 323.15) K
- Equilibrium solubility of carbon dioxide in aqueous 2-((2-aminoethyl)amino)ethanol and N-methyldiethanolamine solution and modeling by electrolyte mPR-CPA EoS
- Excess molar enthalpies for binary mixtures of different amines with water
- Measuring and correlating solubility of hydrogen sulfide in aqueous solution of 2-((2 aminoethyl)amino)ethanol
- Experimental Data and Modeling for Viscosity and Refractive Index of Aqueous Mixtures with 2-(Methylamino)ethanol (MAE) and Aminoethylethanolamine (AEEA)
- Volumetric Properties, Viscosities, and Refractive Indices for Aqueous 2-((2-Aminoethyl)amino)ethanol Solutions from (298.15 to 343.15) K
- Molar Heat Capacity of Various Aqueous Alkanolamine Solutions from 303.15 K to 353.15 K