- Name
- 1,2-Ethanediamine, N-(2-aminoethyl)-
- InChI
- InChI=1S/C4H13N3/c5-1-3-7-4-2-6/h7H,1-6H2
- InChI Key
- RPNUMPOLZDHAAY-UHFFFAOYSA-N
- Formula
- C4H13N3
- SMILES
- NCCNCCN
- Mol. Weight (g/mol)
- 103.17
- CAS
- 111-40-0
- 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
- Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
- η - Viscosity, Pa*s (4)
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (4)
- Binary diffusion coefficient, m2/s (2)
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 303.15 | 0.1043 | 99.50 |
| 308.15 | 0.1043 | 100.30 |
| 313.15 | 0.1043 | 101.80 |
| 318.15 | 0.1043 | 101.80 |
| 323.15 | 0.1043 | 102.30 |
| 328.15 | 0.1043 | 102.90 |
| 333.15 | 0.1043 | 103.30 |
| 338.15 | 0.1043 | 103.70 |
| 343.15 | 0.1043 | 104.20 |
| 348.15 | 0.1043 | 105.00 |
| 353.15 | 0.1043 | 105.40 |
| 303.15 | 0.1487 | 110.20 |
| 308.15 | 0.1487 | 111.30 |
| 313.15 | 0.1487 | 112.40 |
| 318.15 | 0.1487 | 113.40 |
| 323.15 | 0.1487 | 114.40 |
| 328.15 | 0.1487 | 115.10 |
| 333.15 | 0.1487 | 115.70 |
| 338.15 | 0.1487 | 116.10 |
| 343.15 | 0.1487 | 116.80 |
| 348.15 | 0.1487 | 117.90 |
| 353.15 | 0.1487 | 119.00 |
| 303.15 | 0.2076 | 124.70 |
| 308.15 | 0.2076 | 126.10 |
| 313.15 | 0.2076 | 127.40 |
| 318.15 | 0.2076 | 128.60 |
| 323.15 | 0.2076 | 129.90 |
| 328.15 | 0.2076 | 130.90 |
| 333.15 | 0.2076 | 132.00 |
| 338.15 | 0.2076 | 133.00 |
| 343.15 | 0.2076 | 133.90 |
| 348.15 | 0.2076 | 134.50 |
| 353.15 | 0.2076 | 135.20 |
| 303.15 | 0.2895 | 144.30 |
| 308.15 | 0.2895 | 145.70 |
| 313.15 | 0.2895 | 146.90 |
| 318.15 | 0.2895 | 148.10 |
| 323.15 | 0.2895 | 149.30 |
| 328.15 | 0.2895 | 150.40 |
| 333.15 | 0.2895 | 151.40 |
| 338.15 | 0.2895 | 152.50 |
| 343.15 | 0.2895 | 153.50 |
| 348.15 | 0.2895 | 154.30 |
| 353.15 | 0.2895 | 155.10 |
| 303.15 | 0.4112 | 170.30 |
| 308.15 | 0.4112 | 171.50 |
| 313.15 | 0.4112 | 172.70 |
| 318.15 | 0.4112 | 173.90 |
| 323.15 | 0.4112 | 175.20 |
| 328.15 | 0.4112 | 176.20 |
| 333.15 | 0.4112 | 177.30 |
| 338.15 | 0.4112 | 178.50 |
| 343.15 | 0.4112 | 179.50 |
| 348.15 | 0.4112 | 180.40 |
| 353.15 | 0.4112 | 181.30 |
| 303.15 | 0.6111 | 209.10 |
| 308.15 | 0.6111 | 210.00 |
| 313.15 | 0.6111 | 211.20 |
| 318.15 | 0.6111 | 212.20 |
| 323.15 | 0.6111 | 213.40 |
| 328.15 | 0.6111 | 214.20 |
| 333.15 | 0.6111 | 214.70 |
| 338.15 | 0.6111 | 215.40 |
| 343.15 | 0.6111 | 215.90 |
| 348.15 | 0.6111 | 216.30 |
| 353.15 | 0.6111 | 216.50 |
| 303.15 | 0.8000 | 241.30 |
| 308.15 | 0.8000 | 241.90 |
| 313.15 | 0.8000 | 242.70 |
| 318.15 | 0.8000 | 243.40 |
| 323.15 | 0.8000 | 244.00 |
| 328.15 | 0.8000 | 244.70 |
| 333.15 | 0.8000 | 245.30 |
| 338.15 | 0.8000 | 246.00 |
| 343.15 | 0.8000 | 246.40 |
| 348.15 | 0.8000 | 247.10 |
| 353.15 | 0.8000 | 247.40 |
| 303.15 | 1.0000 | 269.50 |
| 308.15 | 1.0000 | 269.90 |
| 313.15 | 1.0000 | 270.20 |
| 318.15 | 1.0000 | 270.80 |
| 323.15 | 1.0000 | 271.20 |
| 328.15 | 1.0000 | 272.00 |
| 333.15 | 1.0000 | 272.70 |
| 338.15 | 1.0000 | 273.20 |
| 343.15 | 1.0000 | 273.60 |
| 348.15 | 1.0000 | 273.80 |
| 353.15 | 1.0000 | 274.00 |
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 303.15 | 0.1043 | 99.50 |
| 308.15 | 0.1043 | 100.30 |
| 313.15 | 0.1043 | 101.80 |
| 318.15 | 0.1043 | 101.80 |
| 323.15 | 0.1043 | 102.30 |
| 328.15 | 0.1043 | 102.90 |
| 333.15 | 0.1043 | 103.30 |
| 338.15 | 0.1043 | 103.70 |
| 343.15 | 0.1043 | 104.20 |
| 348.15 | 0.1043 | 105.00 |
| 353.15 | 0.1043 | 105.40 |
| 303.15 | 0.1487 | 110.20 |
| 308.15 | 0.1487 | 111.30 |
| 313.15 | 0.1487 | 112.40 |
| 318.15 | 0.1487 | 113.40 |
| 323.15 | 0.1487 | 114.40 |
| 328.15 | 0.1487 | 115.10 |
| 333.15 | 0.1487 | 115.70 |
| 338.15 | 0.1487 | 116.10 |
| 343.15 | 0.1487 | 116.80 |
| 348.15 | 0.1487 | 117.90 |
| 353.15 | 0.1487 | 119.00 |
| 303.15 | 0.2076 | 124.70 |
| 308.15 | 0.2076 | 126.10 |
| 313.15 | 0.2076 | 127.40 |
| 318.15 | 0.2076 | 128.60 |
| 323.15 | 0.2076 | 129.90 |
| 328.15 | 0.2076 | 130.90 |
| 333.15 | 0.2076 | 132.00 |
| 338.15 | 0.2076 | 133.00 |
| 343.15 | 0.2076 | 133.90 |
| 348.15 | 0.2076 | 134.50 |
| 353.15 | 0.2076 | 135.20 |
| 303.15 | 0.2895 | 144.30 |
| 308.15 | 0.2895 | 145.70 |
| 313.15 | 0.2895 | 146.90 |
| 318.15 | 0.2895 | 148.10 |
| 323.15 | 0.2895 | 149.30 |
| 328.15 | 0.2895 | 150.40 |
| 333.15 | 0.2895 | 151.40 |
| 338.15 | 0.2895 | 152.50 |
| 343.15 | 0.2895 | 153.50 |
| 348.15 | 0.2895 | 154.30 |
| 353.15 | 0.2895 | 155.10 |
| 303.15 | 0.4112 | 170.30 |
| 308.15 | 0.4112 | 171.50 |
| 313.15 | 0.4112 | 172.70 |
| 318.15 | 0.4112 | 173.90 |
| 323.15 | 0.4112 | 175.20 |
| 328.15 | 0.4112 | 176.20 |
| 333.15 | 0.4112 | 177.30 |
| 338.15 | 0.4112 | 178.50 |
| 343.15 | 0.4112 | 179.50 |
| 348.15 | 0.4112 | 180.40 |
| 353.15 | 0.4112 | 181.30 |
| 303.15 | 0.6111 | 209.10 |
| 308.15 | 0.6111 | 210.00 |
| 313.15 | 0.6111 | 211.20 |
| 318.15 | 0.6111 | 212.20 |
| 323.15 | 0.6111 | 213.40 |
| 328.15 | 0.6111 | 214.20 |
| 333.15 | 0.6111 | 214.70 |
| 338.15 | 0.6111 | 215.40 |
| 343.15 | 0.6111 | 215.90 |
| 348.15 | 0.6111 | 216.30 |
| 353.15 | 0.6111 | 216.50 |
| 303.15 | 0.8000 | 241.30 |
| 308.15 | 0.8000 | 241.90 |
| 313.15 | 0.8000 | 242.70 |
| 318.15 | 0.8000 | 243.40 |
| 323.15 | 0.8000 | 244.00 |
| 328.15 | 0.8000 | 244.70 |
| 333.15 | 0.8000 | 245.30 |
| 338.15 | 0.8000 | 246.00 |
| 343.15 | 0.8000 | 246.40 |
| 348.15 | 0.8000 | 247.10 |
| 353.15 | 0.8000 | 247.40 |
| 303.15 | 1.0000 | 269.50 |
| 308.15 | 1.0000 | 269.90 |
| 313.15 | 1.0000 | 270.20 |
| 318.15 | 1.0000 | 270.80 |
| 323.15 | 1.0000 | 271.20 |
| 328.15 | 1.0000 | 272.00 |
| 333.15 | 1.0000 | 272.70 |
| 338.15 | 1.0000 | 273.20 |
| 343.15 | 1.0000 | 273.60 |
| 348.15 | 1.0000 | 273.80 |
| 353.15 | 1.0000 | 274.00 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 0.1000 | 303.15 | 0.0012 |
| 0.1000 | 308.15 | 0.0011 |
| 0.1000 | 313.15 | 0.0010 |
| 0.1000 | 318.15 | 0.0009 |
| 0.1000 | 323.15 | 0.0008 |
| 0.2000 | 303.15 | 0.0020 |
| 0.2000 | 308.15 | 0.0018 |
| 0.2000 | 313.15 | 0.0015 |
| 0.2000 | 318.15 | 0.0014 |
| 0.2000 | 323.15 | 0.0012 |
| 0.3000 | 303.15 | 0.0036 |
| 0.3000 | 308.15 | 0.0030 |
| 0.3000 | 313.15 | 0.0026 |
| 0.3000 | 318.15 | 0.0022 |
| 0.3000 | 323.15 | 0.0019 |
| 0.4000 | 303.15 | 0.0073 |
| 0.4000 | 308.15 | 0.0059 |
| 0.4000 | 313.15 | 0.0049 |
| 0.4000 | 318.15 | 0.0040 |
| 0.4000 | 323.15 | 0.0033 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0010 |
| 293.15 | 0.0095 | 0.0013 |
| 293.15 | 0.0299 | 0.0021 |
| 293.15 | 0.0565 | 0.0040 |
| 293.15 | 0.0696 | 0.0054 |
| 293.15 | 0.1043 | 0.0116 |
| 293.15 | 0.1250 | 0.0179 |
| 293.15 | 0.1591 | 0.0311 |
| 293.15 | 0.2076 | 0.0507 |
| 293.15 | 0.2449 | 0.0596 |
| 293.15 | 0.3099 | 0.0594 |
| 293.15 | 0.3438 | 0.0555 |
| 293.15 | 0.4112 | 0.0431 |
| 293.15 | 0.4974 | 0.0301 |
| 293.15 | 0.6111 | 0.0195 |
| 293.15 | 0.6988 | 0.0151 |
| 293.15 | 0.8073 | 0.0106 |
| 293.15 | 0.8954 | 0.0085 |
| 293.15 | 1.0000 | 0.0070 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.0095 | 0.0010 |
| 303.15 | 0.0299 | 0.0016 |
| 303.15 | 0.0565 | 0.0028 |
| 303.15 | 0.0696 | 0.0037 |
| 303.15 | 0.1043 | 0.0073 |
| 303.15 | 0.1250 | 0.0106 |
| 303.15 | 0.1591 | 0.0169 |
| 303.15 | 0.2076 | 0.0256 |
| 303.15 | 0.2449 | 0.0295 |
| 303.15 | 0.3099 | 0.0295 |
| 303.15 | 0.3438 | 0.0280 |
| 303.15 | 0.4112 | 0.0227 |
| 303.15 | 0.4974 | 0.0168 |
| 303.15 | 0.6111 | 0.0115 |
| 303.15 | 0.6988 | 0.0091 |
| 303.15 | 0.8073 | 0.0069 |
| 303.15 | 0.8954 | 0.0057 |
| 303.15 | 1.0000 | 0.0048 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.0095 | 0.0008 |
| 313.15 | 0.0299 | 0.0012 |
| 313.15 | 0.0565 | 0.0021 |
| 313.15 | 0.0696 | 0.0027 |
| 313.15 | 0.1043 | 0.0049 |
| 313.15 | 0.1250 | 0.0067 |
| 313.15 | 0.1591 | 0.0101 |
| 313.15 | 0.2076 | 0.0143 |
| 313.15 | 0.2449 | 0.0162 |
| 313.15 | 0.3099 | 0.0163 |
| 313.15 | 0.3438 | 0.0156 |
| 313.15 | 0.4112 | 0.0130 |
| 313.15 | 0.4974 | 0.0102 |
| 313.15 | 0.6111 | 0.0074 |
| 313.15 | 0.6988 | 0.0059 |
| 313.15 | 0.8073 | 0.0047 |
| 313.15 | 0.8954 | 0.0040 |
| 313.15 | 1.0000 | 0.0034 |
| 323.15 | 0.0000 | 0.0005 |
| 323.15 | 0.0095 | 0.0007 |
| 323.15 | 0.0299 | 0.0010 |
| 323.15 | 0.0565 | 0.0016 |
| 323.15 | 0.0696 | 0.0020 |
| 323.15 | 0.1043 | 0.0034 |
| 323.15 | 0.1250 | 0.0045 |
| 323.15 | 0.1591 | 0.0065 |
| 323.15 | 0.2076 | 0.0087 |
| 323.15 | 0.2449 | 0.0097 |
| 323.15 | 0.3099 | 0.0098 |
| 323.15 | 0.3438 | 0.0095 |
| 323.15 | 0.4112 | 0.0081 |
| 323.15 | 0.4974 | 0.0066 |
| 323.15 | 0.6111 | 0.0050 |
| 323.15 | 0.6988 | 0.0042 |
| 323.15 | 0.8073 | 0.0034 |
| 323.15 | 0.8954 | 0.0030 |
| 323.15 | 1.0000 | 0.0027 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.0095 | 0.0006 |
| 333.15 | 0.0299 | 0.0008 |
| 333.15 | 0.0565 | 0.0013 |
| 333.15 | 0.0696 | 0.0016 |
| 333.15 | 0.1043 | 0.0025 |
| 333.15 | 0.1250 | 0.0032 |
| 333.15 | 0.1591 | 0.0044 |
| 333.15 | 0.2076 | 0.0057 |
| 333.15 | 0.2449 | 0.0063 |
| 333.15 | 0.3099 | 0.0064 |
| 333.15 | 0.3438 | 0.0062 |
| 333.15 | 0.4112 | 0.0054 |
| 333.15 | 0.4974 | 0.0046 |
| 333.15 | 0.6111 | 0.0036 |
| 333.15 | 0.6988 | 0.0031 |
| 333.15 | 0.8073 | 0.0026 |
| 333.15 | 0.8954 | 0.0023 |
| 333.15 | 1.0000 | 0.0021 |
| 343.15 | 0.0000 | 0.0004 |
| 343.15 | 0.0095 | 0.0005 |
| 343.15 | 0.0299 | 0.0007 |
| 343.15 | 0.0565 | 0.0010 |
| 343.15 | 0.0696 | 0.0012 |
| 343.15 | 0.1043 | 0.0019 |
| 343.15 | 0.1250 | 0.0024 |
| 343.15 | 0.1591 | 0.0032 |
| 343.15 | 0.2076 | 0.0039 |
| 343.15 | 0.2449 | 0.0043 |
| 343.15 | 0.3099 | 0.0044 |
| 343.15 | 0.3438 | 0.0043 |
| 343.15 | 0.4112 | 0.0038 |
| 343.15 | 0.4974 | 0.0033 |
| 343.15 | 0.6111 | 0.0027 |
| 343.15 | 0.6988 | 0.0024 |
| 343.15 | 0.8073 | 0.0021 |
| 343.15 | 0.8954 | 0.0018 |
| 343.15 | 1.0000 | 0.0017 |
| 353.15 | 0.0000 | 0.0004 |
| 353.15 | 0.0095 | 0.0004 |
| 353.15 | 0.0299 | 0.0006 |
| 353.15 | 0.0565 | 0.0009 |
| 353.15 | 0.0696 | 0.0010 |
| 353.15 | 0.1043 | 0.0015 |
| 353.15 | 0.1250 | 0.0018 |
| 353.15 | 0.1591 | 0.0024 |
| 353.15 | 0.2076 | 0.0029 |
| 353.15 | 0.2449 | 0.0031 |
| 353.15 | 0.3099 | 0.0032 |
| 353.15 | 0.3438 | 0.0031 |
| 353.15 | 0.4112 | 0.0028 |
| 353.15 | 0.4974 | 0.0025 |
| 353.15 | 0.6111 | 0.0021 |
| 353.15 | 0.6988 | 0.0019 |
| 353.15 | 0.8073 | 0.0017 |
| 353.15 | 0.8954 | 0.0015 |
| 353.15 | 1.0000 | 0.0014 |
| 363.15 | 0.0000 | 0.0003 |
| 363.15 | 0.0095 | 0.0004 |
| 363.15 | 0.0299 | 0.0005 |
| 363.15 | 0.0565 | 0.0007 |
| 363.15 | 0.0696 | 0.0008 |
| 363.15 | 0.1043 | 0.0012 |
| 363.15 | 0.1250 | 0.0014 |
| 363.15 | 0.1591 | 0.0018 |
| 363.15 | 0.2076 | 0.0021 |
| 363.15 | 0.2449 | 0.0023 |
| 363.15 | 0.3099 | 0.0024 |
| 363.15 | 0.3438 | 0.0023 |
| 363.15 | 0.4112 | 0.0022 |
| 363.15 | 0.4974 | 0.0020 |
| 363.15 | 0.6111 | 0.0017 |
| 363.15 | 0.6988 | 0.0015 |
| 363.15 | 0.8073 | 0.0014 |
| 363.15 | 0.8954 | 0.0013 |
| 363.15 | 1.0000 | 0.0012 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 0.1000 | 303.15 | 0.0012 |
| 0.1000 | 308.15 | 0.0011 |
| 0.1000 | 313.15 | 0.0010 |
| 0.1000 | 318.15 | 0.0009 |
| 0.1000 | 323.15 | 0.0008 |
| 0.2000 | 303.15 | 0.0020 |
| 0.2000 | 308.15 | 0.0018 |
| 0.2000 | 313.15 | 0.0015 |
| 0.2000 | 318.15 | 0.0014 |
| 0.2000 | 323.15 | 0.0012 |
| 0.3000 | 303.15 | 0.0036 |
| 0.3000 | 308.15 | 0.0030 |
| 0.3000 | 313.15 | 0.0026 |
| 0.3000 | 318.15 | 0.0022 |
| 0.3000 | 323.15 | 0.0019 |
| 0.4000 | 303.15 | 0.0073 |
| 0.4000 | 308.15 | 0.0059 |
| 0.4000 | 313.15 | 0.0049 |
| 0.4000 | 318.15 | 0.0040 |
| 0.4000 | 323.15 | 0.0033 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0010 |
| 293.15 | 0.0095 | 0.0013 |
| 293.15 | 0.0299 | 0.0021 |
| 293.15 | 0.0565 | 0.0040 |
| 293.15 | 0.0696 | 0.0054 |
| 293.15 | 0.1043 | 0.0116 |
| 293.15 | 0.1250 | 0.0179 |
| 293.15 | 0.1591 | 0.0311 |
| 293.15 | 0.2076 | 0.0507 |
| 293.15 | 0.2449 | 0.0596 |
| 293.15 | 0.3099 | 0.0594 |
| 293.15 | 0.3438 | 0.0555 |
| 293.15 | 0.4112 | 0.0431 |
| 293.15 | 0.4974 | 0.0301 |
| 293.15 | 0.6111 | 0.0195 |
| 293.15 | 0.6988 | 0.0151 |
| 293.15 | 0.8073 | 0.0106 |
| 293.15 | 0.8954 | 0.0085 |
| 293.15 | 1.0000 | 0.0070 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.0095 | 0.0010 |
| 303.15 | 0.0299 | 0.0016 |
| 303.15 | 0.0565 | 0.0028 |
| 303.15 | 0.0696 | 0.0037 |
| 303.15 | 0.1043 | 0.0073 |
| 303.15 | 0.1250 | 0.0106 |
| 303.15 | 0.1591 | 0.0169 |
| 303.15 | 0.2076 | 0.0256 |
| 303.15 | 0.2449 | 0.0295 |
| 303.15 | 0.3099 | 0.0295 |
| 303.15 | 0.3438 | 0.0280 |
| 303.15 | 0.4112 | 0.0227 |
| 303.15 | 0.4974 | 0.0168 |
| 303.15 | 0.6111 | 0.0115 |
| 303.15 | 0.6988 | 0.0091 |
| 303.15 | 0.8073 | 0.0069 |
| 303.15 | 0.8954 | 0.0057 |
| 303.15 | 1.0000 | 0.0048 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.0095 | 0.0008 |
| 313.15 | 0.0299 | 0.0012 |
| 313.15 | 0.0565 | 0.0021 |
| 313.15 | 0.0696 | 0.0027 |
| 313.15 | 0.1043 | 0.0049 |
| 313.15 | 0.1250 | 0.0067 |
| 313.15 | 0.1591 | 0.0101 |
| 313.15 | 0.2076 | 0.0143 |
| 313.15 | 0.2449 | 0.0162 |
| 313.15 | 0.3099 | 0.0163 |
| 313.15 | 0.3438 | 0.0156 |
| 313.15 | 0.4112 | 0.0130 |
| 313.15 | 0.4974 | 0.0102 |
| 313.15 | 0.6111 | 0.0074 |
| 313.15 | 0.6988 | 0.0059 |
| 313.15 | 0.8073 | 0.0047 |
| 313.15 | 0.8954 | 0.0040 |
| 313.15 | 1.0000 | 0.0034 |
| 323.15 | 0.0000 | 0.0005 |
| 323.15 | 0.0095 | 0.0007 |
| 323.15 | 0.0299 | 0.0010 |
| 323.15 | 0.0565 | 0.0016 |
| 323.15 | 0.0696 | 0.0020 |
| 323.15 | 0.1043 | 0.0034 |
| 323.15 | 0.1250 | 0.0045 |
| 323.15 | 0.1591 | 0.0065 |
| 323.15 | 0.2076 | 0.0087 |
| 323.15 | 0.2449 | 0.0097 |
| 323.15 | 0.3099 | 0.0098 |
| 323.15 | 0.3438 | 0.0095 |
| 323.15 | 0.4112 | 0.0081 |
| 323.15 | 0.4974 | 0.0066 |
| 323.15 | 0.6111 | 0.0050 |
| 323.15 | 0.6988 | 0.0042 |
| 323.15 | 0.8073 | 0.0034 |
| 323.15 | 0.8954 | 0.0030 |
| 323.15 | 1.0000 | 0.0027 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.0095 | 0.0006 |
| 333.15 | 0.0299 | 0.0008 |
| 333.15 | 0.0565 | 0.0013 |
| 333.15 | 0.0696 | 0.0016 |
| 333.15 | 0.1043 | 0.0025 |
| 333.15 | 0.1250 | 0.0032 |
| 333.15 | 0.1591 | 0.0044 |
| 333.15 | 0.2076 | 0.0057 |
| 333.15 | 0.2449 | 0.0063 |
| 333.15 | 0.3099 | 0.0064 |
| 333.15 | 0.3438 | 0.0062 |
| 333.15 | 0.4112 | 0.0054 |
| 333.15 | 0.4974 | 0.0046 |
| 333.15 | 0.6111 | 0.0036 |
| 333.15 | 0.6988 | 0.0031 |
| 333.15 | 0.8073 | 0.0026 |
| 333.15 | 0.8954 | 0.0023 |
| 333.15 | 1.0000 | 0.0021 |
| 343.15 | 0.0000 | 0.0004 |
| 343.15 | 0.0095 | 0.0005 |
| 343.15 | 0.0299 | 0.0007 |
| 343.15 | 0.0565 | 0.0010 |
| 343.15 | 0.0696 | 0.0012 |
| 343.15 | 0.1043 | 0.0019 |
| 343.15 | 0.1250 | 0.0024 |
| 343.15 | 0.1591 | 0.0032 |
| 343.15 | 0.2076 | 0.0039 |
| 343.15 | 0.2449 | 0.0043 |
| 343.15 | 0.3099 | 0.0044 |
| 343.15 | 0.3438 | 0.0043 |
| 343.15 | 0.4112 | 0.0038 |
| 343.15 | 0.4974 | 0.0033 |
| 343.15 | 0.6111 | 0.0027 |
| 343.15 | 0.6988 | 0.0024 |
| 343.15 | 0.8073 | 0.0021 |
| 343.15 | 0.8954 | 0.0018 |
| 343.15 | 1.0000 | 0.0017 |
| 353.15 | 0.0000 | 0.0004 |
| 353.15 | 0.0095 | 0.0004 |
| 353.15 | 0.0299 | 0.0006 |
| 353.15 | 0.0565 | 0.0009 |
| 353.15 | 0.0696 | 0.0010 |
| 353.15 | 0.1043 | 0.0015 |
| 353.15 | 0.1250 | 0.0018 |
| 353.15 | 0.1591 | 0.0024 |
| 353.15 | 0.2076 | 0.0029 |
| 353.15 | 0.2449 | 0.0031 |
| 353.15 | 0.3099 | 0.0032 |
| 353.15 | 0.3438 | 0.0031 |
| 353.15 | 0.4112 | 0.0028 |
| 353.15 | 0.4974 | 0.0025 |
| 353.15 | 0.6111 | 0.0021 |
| 353.15 | 0.6988 | 0.0019 |
| 353.15 | 0.8073 | 0.0017 |
| 353.15 | 0.8954 | 0.0015 |
| 353.15 | 1.0000 | 0.0014 |
| 363.15 | 0.0000 | 0.0003 |
| 363.15 | 0.0095 | 0.0004 |
| 363.15 | 0.0299 | 0.0005 |
| 363.15 | 0.0565 | 0.0007 |
| 363.15 | 0.0696 | 0.0008 |
| 363.15 | 0.1043 | 0.0012 |
| 363.15 | 0.1250 | 0.0014 |
| 363.15 | 0.1591 | 0.0018 |
| 363.15 | 0.2076 | 0.0021 |
| 363.15 | 0.2449 | 0.0023 |
| 363.15 | 0.3099 | 0.0024 |
| 363.15 | 0.3438 | 0.0023 |
| 363.15 | 0.4112 | 0.0022 |
| 363.15 | 0.4974 | 0.0020 |
| 363.15 | 0.6111 | 0.0017 |
| 363.15 | 0.6988 | 0.0015 |
| 363.15 | 0.8073 | 0.0014 |
| 363.15 | 0.8954 | 0.0013 |
| 363.15 | 1.0000 | 0.0012 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 303.15 | 0.0509 | -2.269 |
| 303.15 | 0.1001 | -4.104 |
| 303.15 | 0.1544 | -5.559 |
| 303.15 | 0.1962 | -6.204 |
| 303.15 | 0.2416 | -6.523 |
| 303.15 | 0.3018 | -6.647 |
| 303.15 | 0.4026 | -6.356 |
| 303.15 | 0.5010 | -5.417 |
| 303.15 | 0.6025 | -4.412 |
| 303.15 | 0.7020 | -3.393 |
| 303.15 | 0.7984 | -2.383 |
| 323.15 | 0.0503 | -2.11 |
| 323.15 | 0.0989 | -3.81 |
| 323.15 | 0.2028 | -5.882 |
| 323.15 | 0.3003 | -6.307 |
| 323.15 | 0.4044 | -5.777 |
| 323.15 | 0.5100 | -5.059 |
| 323.15 | 0.6027 | -3.925 |
| 323.15 | 0.7018 | -3.19 |
| 323.15 | 0.7983 | -2.142 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 303.15 | 0.0509 | -2.269 |
| 303.15 | 0.1001 | -4.104 |
| 303.15 | 0.1544 | -5.559 |
| 303.15 | 0.1962 | -6.204 |
| 303.15 | 0.2416 | -6.523 |
| 303.15 | 0.3018 | -6.647 |
| 303.15 | 0.4026 | -6.356 |
| 303.15 | 0.5010 | -5.417 |
| 303.15 | 0.6025 | -4.412 |
| 303.15 | 0.7020 | -3.393 |
| 303.15 | 0.7984 | -2.383 |
| 323.15 | 0.0503 | -2.11 |
| 323.15 | 0.0989 | -3.81 |
| 323.15 | 0.2028 | -5.882 |
| 323.15 | 0.3003 | -6.307 |
| 323.15 | 0.4044 | -5.777 |
| 323.15 | 0.5100 | -5.059 |
| 323.15 | 0.6027 | -3.925 |
| 323.15 | 0.7018 | -3.19 |
| 323.15 | 0.7983 | -2.142 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.1000 | 303.15 | 998.5 |
| 0.1000 | 308.15 | 996.7 |
| 0.1000 | 313.15 | 994.8 |
| 0.1000 | 318.15 | 992.8 |
| 0.1000 | 323.15 | 990.6 |
| 0.2000 | 303.15 | 1002.9 |
| 0.2000 | 308.15 | 1000.8 |
| 0.2000 | 313.15 | 998.7 |
| 0.2000 | 318.15 | 996.3 |
| 0.2000 | 323.15 | 993.9 |
| 0.3000 | 303.15 | 1009.8 |
| 0.3000 | 308.15 | 1007.2 |
| 0.3000 | 313.15 | 1004.5 |
| 0.3000 | 318.15 | 1001.8 |
| 0.3000 | 323.15 | 998.9 |
| 0.4000 | 303.15 | 1016.2 |
| 0.4000 | 308.15 | 1013.0 |
| 0.4000 | 313.15 | 1009.9 |
| 0.4000 | 318.15 | 1006.7 |
| 0.4000 | 323.15 | 1003.4 |
| 1.0000 | 303.15 | 942.1 |
| 1.0000 | 308.15 | 937.9 |
| 1.0000 | 313.15 | 933.8 |
| 1.0000 | 318.15 | 929.6 |
| 1.0000 | 323.15 | 925.5 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 999.2 |
| 293.15 | 0.0095 | 1001.5 |
| 293.15 | 0.0299 | 1004.2 |
| 293.15 | 0.0565 | 1011.5 |
| 293.15 | 0.0696 | 1014.5 |
| 293.15 | 0.1043 | 1023.8 |
| 293.15 | 0.1250 | 1026.5 |
| 293.15 | 0.1591 | 1030.7 |
| 293.15 | 0.2076 | 1029.4 |
| 293.15 | 0.2449 | 1027.5 |
| 293.15 | 0.3099 | 1019.1 |
| 293.15 | 0.3438 | 1014.1 |
| 293.15 | 0.4112 | 1004.1 |
| 293.15 | 0.4974 | 992.8 |
| 293.15 | 0.6111 | 979.0 |
| 293.15 | 0.6988 | 971.8 |
| 293.15 | 0.8073 | 963.4 |
| 293.15 | 0.8954 | 957.5 |
| 293.15 | 1.0000 | 951.0 |
| 303.15 | 0.0000 | 996.5 |
| 303.15 | 0.0095 | 998.6 |
| 303.15 | 0.0299 | 1000.7 |
| 303.15 | 0.0565 | 1007.1 |
| 303.15 | 0.0696 | 1009.6 |
| 303.15 | 0.1043 | 1017.1 |
| 303.15 | 0.1250 | 1019.8 |
| 303.15 | 0.1591 | 1023.0 |
| 303.15 | 0.2076 | 1021.4 |
| 303.15 | 0.2449 | 1018.6 |
| 303.15 | 0.3099 | 1010.2 |
| 303.15 | 0.3438 | 1005.7 |
| 303.15 | 0.4112 | 995.0 |
| 303.15 | 0.4974 | 983.7 |
| 303.15 | 0.6111 | 970.6 |
| 303.15 | 0.6988 | 962.7 |
| 303.15 | 0.8073 | 954.3 |
| 303.15 | 0.8954 | 948.4 |
| 303.15 | 1.0000 | 942.3 |
| 313.15 | 0.0000 | 993.0 |
| 313.15 | 0.0095 | 994.9 |
| 313.15 | 0.0299 | 996.7 |
| 313.15 | 0.0565 | 1002.2 |
| 313.15 | 0.0696 | 1004.3 |
| 313.15 | 0.1043 | 1010.7 |
| 313.15 | 0.1250 | 1012.9 |
| 313.15 | 0.1591 | 1015.4 |
| 313.15 | 0.2076 | 1013.2 |
| 313.15 | 0.2449 | 1009.9 |
| 313.15 | 0.3099 | 1001.5 |
| 313.15 | 0.3438 | 997.1 |
| 313.15 | 0.4112 | 986.4 |
| 313.15 | 0.4974 | 975.1 |
| 313.15 | 0.6111 | 962.1 |
| 313.15 | 0.6988 | 954.2 |
| 313.15 | 0.8073 | 947.3 |
| 313.15 | 0.8954 | 939.8 |
| 313.15 | 1.0000 | 933.8 |
| 323.15 | 0.0000 | 988.7 |
| 323.15 | 0.0095 | 990.5 |
| 323.15 | 0.0299 | 991.7 |
| 323.15 | 0.0565 | 996.8 |
| 323.15 | 0.0696 | 998.6 |
| 323.15 | 0.1043 | 1004.2 |
| 323.15 | 0.1250 | 1005.7 |
| 323.15 | 0.1591 | 1007.9 |
| 323.15 | 0.2076 | 1004.8 |
| 323.15 | 0.2449 | 1001.9 |
| 323.15 | 0.3099 | 993.1 |
| 323.15 | 0.3438 | 988.4 |
| 323.15 | 0.4112 | 978.0 |
| 323.15 | 0.4974 | 966.8 |
| 323.15 | 0.6111 | 953.7 |
| 323.15 | 0.6988 | 945.9 |
| 323.15 | 0.8073 | 939.1 |
| 323.15 | 0.8954 | 931.5 |
| 323.15 | 1.0000 | 925.5 |
| 333.15 | 0.0000 | 983.7 |
| 333.15 | 0.0095 | 985.5 |
| 333.15 | 0.0299 | 986.5 |
| 333.15 | 0.0565 | 991.0 |
| 333.15 | 0.0696 | 992.4 |
| 333.15 | 0.1043 | 997.2 |
| 333.15 | 0.1250 | 998.2 |
| 333.15 | 0.1591 | 999.9 |
| 333.15 | 0.2076 | 996.3 |
| 333.15 | 0.2449 | 993.1 |
| 333.15 | 0.3099 | 984.1 |
| 333.15 | 0.3438 | 979.6 |
| 333.15 | 0.4112 | 969.2 |
| 333.15 | 0.4974 | 956.8 |
| 333.15 | 0.6111 | 945.1 |
| 333.15 | 0.6988 | 937.3 |
| 333.15 | 0.8073 | 929.1 |
| 333.15 | 0.8954 | 922.9 |
| 333.15 | 1.0000 | 917.0 |
| 343.15 | 0.0000 | 978.3 |
| 343.15 | 0.0095 | 980.0 |
| 343.15 | 0.0299 | 980.8 |
| 343.15 | 0.0565 | 984.7 |
| 343.15 | 0.0696 | 985.8 |
| 343.15 | 0.1043 | 990.1 |
| 343.15 | 0.1250 | 990.5 |
| 343.15 | 0.1591 | 992.3 |
| 343.15 | 0.2076 | 987.6 |
| 343.15 | 0.2449 | 984.2 |
| 343.15 | 0.3099 | 975.4 |
| 343.15 | 0.3438 | 970.7 |
| 343.15 | 0.4112 | 960.5 |
| 343.15 | 0.4974 | 949.5 |
| 343.15 | 0.6111 | 936.5 |
| 343.15 | 0.6988 | 929.1 |
| 343.15 | 0.8073 | 920.7 |
| 343.15 | 0.8954 | 914.6 |
| 343.15 | 1.0000 | 908.9 |
| 353.15 | 0.0000 | 972.3 |
| 353.15 | 0.0095 | 973.8 |
| 353.15 | 0.0299 | 974.6 |
| 353.15 | 0.0565 | 978.1 |
| 353.15 | 0.0696 | 978.9 |
| 353.15 | 0.1043 | 982.6 |
| 353.15 | 0.1250 | 982.3 |
| 353.15 | 0.1591 | 982.9 |
| 353.15 | 0.2076 | 978.5 |
| 353.15 | 0.2449 | 975.1 |
| 353.15 | 0.3099 | 966.3 |
| 353.15 | 0.3438 | 961.7 |
| 353.15 | 0.4112 | 951.7 |
| 353.15 | 0.4974 | 940.8 |
| 353.15 | 0.6111 | 927.8 |
| 353.15 | 0.6988 | 920.4 |
| 353.15 | 0.8073 | 912.2 |
| 353.15 | 0.8954 | 906.1 |
| 353.15 | 1.0000 | 900.4 |
| 363.15 | 0.0000 | 965.9 |
| 363.15 | 0.0095 | 967.3 |
| 363.15 | 0.0299 | 967.7 |
| 363.15 | 0.0565 | 970.9 |
| 363.15 | 0.0696 | 971.7 |
| 363.15 | 0.1043 | 974.7 |
| 363.15 | 0.1250 | 974.2 |
| 363.15 | 0.1591 | 974.2 |
| 363.15 | 0.2076 | 969.5 |
| 363.15 | 0.2449 | 966.1 |
| 363.15 | 0.3099 | 957.0 |
| 363.15 | 0.3438 | 952.6 |
| 363.15 | 0.4112 | 942.7 |
| 363.15 | 0.4974 | 931.9 |
| 363.15 | 0.6111 | 919.1 |
| 363.15 | 0.6988 | 911.8 |
| 363.15 | 0.8073 | 903.6 |
| 363.15 | 0.8954 | 897.5 |
| 363.15 | 1.0000 | 891.9 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.1000 | 303.15 | 998.5 |
| 0.1000 | 308.15 | 996.7 |
| 0.1000 | 313.15 | 994.8 |
| 0.1000 | 318.15 | 992.8 |
| 0.1000 | 323.15 | 990.6 |
| 0.2000 | 303.15 | 1002.9 |
| 0.2000 | 308.15 | 1000.8 |
| 0.2000 | 313.15 | 998.7 |
| 0.2000 | 318.15 | 996.3 |
| 0.2000 | 323.15 | 993.9 |
| 0.3000 | 303.15 | 1009.8 |
| 0.3000 | 308.15 | 1007.2 |
| 0.3000 | 313.15 | 1004.5 |
| 0.3000 | 318.15 | 1001.8 |
| 0.3000 | 323.15 | 998.9 |
| 0.4000 | 303.15 | 1016.2 |
| 0.4000 | 308.15 | 1013.0 |
| 0.4000 | 313.15 | 1009.9 |
| 0.4000 | 318.15 | 1006.7 |
| 0.4000 | 323.15 | 1003.4 |
| 1.0000 | 303.15 | 942.1 |
| 1.0000 | 308.15 | 937.9 |
| 1.0000 | 313.15 | 933.8 |
| 1.0000 | 318.15 | 929.6 |
| 1.0000 | 323.15 | 925.5 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 999.2 |
| 293.15 | 0.0095 | 1001.5 |
| 293.15 | 0.0299 | 1004.2 |
| 293.15 | 0.0565 | 1011.5 |
| 293.15 | 0.0696 | 1014.5 |
| 293.15 | 0.1043 | 1023.8 |
| 293.15 | 0.1250 | 1026.5 |
| 293.15 | 0.1591 | 1030.7 |
| 293.15 | 0.2076 | 1029.4 |
| 293.15 | 0.2449 | 1027.5 |
| 293.15 | 0.3099 | 1019.1 |
| 293.15 | 0.3438 | 1014.1 |
| 293.15 | 0.4112 | 1004.1 |
| 293.15 | 0.4974 | 992.8 |
| 293.15 | 0.6111 | 979.0 |
| 293.15 | 0.6988 | 971.8 |
| 293.15 | 0.8073 | 963.4 |
| 293.15 | 0.8954 | 957.5 |
| 293.15 | 1.0000 | 951.0 |
| 303.15 | 0.0000 | 996.5 |
| 303.15 | 0.0095 | 998.6 |
| 303.15 | 0.0299 | 1000.7 |
| 303.15 | 0.0565 | 1007.1 |
| 303.15 | 0.0696 | 1009.6 |
| 303.15 | 0.1043 | 1017.1 |
| 303.15 | 0.1250 | 1019.8 |
| 303.15 | 0.1591 | 1023.0 |
| 303.15 | 0.2076 | 1021.4 |
| 303.15 | 0.2449 | 1018.6 |
| 303.15 | 0.3099 | 1010.2 |
| 303.15 | 0.3438 | 1005.7 |
| 303.15 | 0.4112 | 995.0 |
| 303.15 | 0.4974 | 983.7 |
| 303.15 | 0.6111 | 970.6 |
| 303.15 | 0.6988 | 962.7 |
| 303.15 | 0.8073 | 954.3 |
| 303.15 | 0.8954 | 948.4 |
| 303.15 | 1.0000 | 942.3 |
| 313.15 | 0.0000 | 993.0 |
| 313.15 | 0.0095 | 994.9 |
| 313.15 | 0.0299 | 996.7 |
| 313.15 | 0.0565 | 1002.2 |
| 313.15 | 0.0696 | 1004.3 |
| 313.15 | 0.1043 | 1010.7 |
| 313.15 | 0.1250 | 1012.9 |
| 313.15 | 0.1591 | 1015.4 |
| 313.15 | 0.2076 | 1013.2 |
| 313.15 | 0.2449 | 1009.9 |
| 313.15 | 0.3099 | 1001.5 |
| 313.15 | 0.3438 | 997.1 |
| 313.15 | 0.4112 | 986.4 |
| 313.15 | 0.4974 | 975.1 |
| 313.15 | 0.6111 | 962.1 |
| 313.15 | 0.6988 | 954.2 |
| 313.15 | 0.8073 | 947.3 |
| 313.15 | 0.8954 | 939.8 |
| 313.15 | 1.0000 | 933.8 |
| 323.15 | 0.0000 | 988.7 |
| 323.15 | 0.0095 | 990.5 |
| 323.15 | 0.0299 | 991.7 |
| 323.15 | 0.0565 | 996.8 |
| 323.15 | 0.0696 | 998.6 |
| 323.15 | 0.1043 | 1004.2 |
| 323.15 | 0.1250 | 1005.7 |
| 323.15 | 0.1591 | 1007.9 |
| 323.15 | 0.2076 | 1004.8 |
| 323.15 | 0.2449 | 1001.9 |
| 323.15 | 0.3099 | 993.1 |
| 323.15 | 0.3438 | 988.4 |
| 323.15 | 0.4112 | 978.0 |
| 323.15 | 0.4974 | 966.8 |
| 323.15 | 0.6111 | 953.7 |
| 323.15 | 0.6988 | 945.9 |
| 323.15 | 0.8073 | 939.1 |
| 323.15 | 0.8954 | 931.5 |
| 323.15 | 1.0000 | 925.5 |
| 333.15 | 0.0000 | 983.7 |
| 333.15 | 0.0095 | 985.5 |
| 333.15 | 0.0299 | 986.5 |
| 333.15 | 0.0565 | 991.0 |
| 333.15 | 0.0696 | 992.4 |
| 333.15 | 0.1043 | 997.2 |
| 333.15 | 0.1250 | 998.2 |
| 333.15 | 0.1591 | 999.9 |
| 333.15 | 0.2076 | 996.3 |
| 333.15 | 0.2449 | 993.1 |
| 333.15 | 0.3099 | 984.1 |
| 333.15 | 0.3438 | 979.6 |
| 333.15 | 0.4112 | 969.2 |
| 333.15 | 0.4974 | 956.8 |
| 333.15 | 0.6111 | 945.1 |
| 333.15 | 0.6988 | 937.3 |
| 333.15 | 0.8073 | 929.1 |
| 333.15 | 0.8954 | 922.9 |
| 333.15 | 1.0000 | 917.0 |
| 343.15 | 0.0000 | 978.3 |
| 343.15 | 0.0095 | 980.0 |
| 343.15 | 0.0299 | 980.8 |
| 343.15 | 0.0565 | 984.7 |
| 343.15 | 0.0696 | 985.8 |
| 343.15 | 0.1043 | 990.1 |
| 343.15 | 0.1250 | 990.5 |
| 343.15 | 0.1591 | 992.3 |
| 343.15 | 0.2076 | 987.6 |
| 343.15 | 0.2449 | 984.2 |
| 343.15 | 0.3099 | 975.4 |
| 343.15 | 0.3438 | 970.7 |
| 343.15 | 0.4112 | 960.5 |
| 343.15 | 0.4974 | 949.5 |
| 343.15 | 0.6111 | 936.5 |
| 343.15 | 0.6988 | 929.1 |
| 343.15 | 0.8073 | 920.7 |
| 343.15 | 0.8954 | 914.6 |
| 343.15 | 1.0000 | 908.9 |
| 353.15 | 0.0000 | 972.3 |
| 353.15 | 0.0095 | 973.8 |
| 353.15 | 0.0299 | 974.6 |
| 353.15 | 0.0565 | 978.1 |
| 353.15 | 0.0696 | 978.9 |
| 353.15 | 0.1043 | 982.6 |
| 353.15 | 0.1250 | 982.3 |
| 353.15 | 0.1591 | 982.9 |
| 353.15 | 0.2076 | 978.5 |
| 353.15 | 0.2449 | 975.1 |
| 353.15 | 0.3099 | 966.3 |
| 353.15 | 0.3438 | 961.7 |
| 353.15 | 0.4112 | 951.7 |
| 353.15 | 0.4974 | 940.8 |
| 353.15 | 0.6111 | 927.8 |
| 353.15 | 0.6988 | 920.4 |
| 353.15 | 0.8073 | 912.2 |
| 353.15 | 0.8954 | 906.1 |
| 353.15 | 1.0000 | 900.4 |
| 363.15 | 0.0000 | 965.9 |
| 363.15 | 0.0095 | 967.3 |
| 363.15 | 0.0299 | 967.7 |
| 363.15 | 0.0565 | 970.9 |
| 363.15 | 0.0696 | 971.7 |
| 363.15 | 0.1043 | 974.7 |
| 363.15 | 0.1250 | 974.2 |
| 363.15 | 0.1591 | 974.2 |
| 363.15 | 0.2076 | 969.5 |
| 363.15 | 0.2449 | 966.1 |
| 363.15 | 0.3099 | 957.0 |
| 363.15 | 0.3438 | 952.6 |
| 363.15 | 0.4112 | 942.7 |
| 363.15 | 0.4974 | 931.9 |
| 363.15 | 0.6111 | 919.1 |
| 363.15 | 0.6988 | 911.8 |
| 363.15 | 0.8073 | 903.6 |
| 363.15 | 0.8954 | 897.5 |
| 363.15 | 1.0000 | 891.9 |
Binary diffusion coefficient, m2/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Temperature, K - Liquid | Binary diffusion coefficient, m2/s - Liquid |
| 0.0000 | 303.15 | 0.0000 |
| 0.0000 | 308.15 | 0.0000 |
| 0.0000 | 313.15 | 0.0000 |
| 0.0000 | 318.15 | 0.0000 |
| 0.0000 | 323.15 | 0.0000 |
| 0.1000 | 303.15 | 0.0000 |
| 0.1000 | 308.15 | 0.0000 |
| 0.1000 | 313.15 | 0.0000 |
| 0.1000 | 318.15 | 0.0000 |
| 0.1000 | 323.15 | 0.0000 |
| 0.2000 | 303.15 | 0.0000 |
| 0.2000 | 308.15 | 0.0000 |
| 0.2000 | 313.15 | 0.0000 |
| 0.2000 | 318.15 | 0.0000 |
| 0.2000 | 323.15 | 0.0000 |
| 0.3000 | 303.15 | 0.0000 |
| 0.3000 | 308.15 | 0.0000 |
| 0.3000 | 313.15 | 0.0000 |
| 0.3000 | 318.15 | 0.0000 |
| 0.3000 | 323.15 | 0.0000 |
| 0.4000 | 303.15 | 0.0000 |
| 0.4000 | 308.15 | 0.0000 |
| 0.4000 | 313.15 | 0.0000 |
| 0.4000 | 318.15 | 0.0000 |
| 0.4000 | 323.15 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mass fraction of 1,2-Ethanediamine, N-(2-aminoethyl)- (1) - Liquid | Temperature, K - Liquid | Binary diffusion coefficient, m2/s - Liquid |
| 0.0000 | 303.15 | 0.0000 |
| 0.0000 | 308.15 | 0.0000 |
| 0.0000 | 313.15 | 0.0000 |
| 0.0000 | 318.15 | 0.0000 |
| 0.0000 | 323.15 | 0.0000 |
| 0.1000 | 303.15 | 0.0000 |
| 0.1000 | 308.15 | 0.0000 |
| 0.1000 | 313.15 | 0.0000 |
| 0.1000 | 318.15 | 0.0000 |
| 0.1000 | 323.15 | 0.0000 |
| 0.2000 | 303.15 | 0.0000 |
| 0.2000 | 308.15 | 0.0000 |
| 0.2000 | 313.15 | 0.0000 |
| 0.2000 | 318.15 | 0.0000 |
| 0.2000 | 323.15 | 0.0000 |
| 0.3000 | 303.15 | 0.0000 |
| 0.3000 | 308.15 | 0.0000 |
| 0.3000 | 313.15 | 0.0000 |
| 0.3000 | 318.15 | 0.0000 |
| 0.3000 | 323.15 | 0.0000 |
| 0.4000 | 303.15 | 0.0000 |
| 0.4000 | 308.15 | 0.0000 |
| 0.4000 | 313.15 | 0.0000 |
| 0.4000 | 318.15 | 0.0000 |
| 0.4000 | 323.15 | 0.0000 |
Sources
- Mutual diffusion coefficients, density, and viscosity of aqueoussolutions of new polyamine CO2absorbents
- Density, viscosity, and excess properties of aqueous solution of diethylenetriamine (DETA)
- Excess molar enthalpies for binary mixtures of different amines with water
- Molar heat capacities of diethylenetriamine and 3-(methylamino)propylamine, their aqueous binaries, and aqueous ternaries with piperazine