- Name
- Ethanamine, N-ethyl-
- InChI
- InChI=1S/C4H11N/c1-3-5-4-2/h5H,3-4H2,1-2H3
- InChI Key
- HPNMFZURTQLUMO-UHFFFAOYSA-N
- Formula
- C4H11N
- SMILES
- CCNCC
- Mol. Weight (g/mol)
- 73.14
- CAS
- 109-89-7
- Name
- 1-Decanol
- InChI
- InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3
- InChI Key
- MWKFXSUHUHTGQN-UHFFFAOYSA-N
- Formula
- C10H22O
- SMILES
- CCCCCCCCCCO
- Mol. Weight (g/mol)
- 158.28
- CAS
- 112-30-1
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
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanamine, N-ethyl- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.00 | 0.0000 | 0.0134 |
| 293.00 | 0.0989 | 0.0110 |
| 293.00 | 0.1963 | 0.0090 |
| 293.00 | 0.3062 | 0.0071 |
| 293.00 | 0.4062 | 0.0054 |
| 293.00 | 0.4898 | 0.0039 |
| 293.00 | 0.5973 | 0.0026 |
| 293.00 | 0.6708 | 0.0019 |
| 293.00 | 0.7388 | 0.0014 |
| 293.00 | 0.8012 | 0.0011 |
| 293.00 | 0.8562 | 0.0008 |
| 293.00 | 0.9031 | 0.0006 |
| 293.00 | 0.9601 | 0.0004 |
| 293.00 | 1.0000 | 0.0003 |
| 303.00 | 0.0000 | 0.0093 |
| 303.00 | 0.0989 | 0.0078 |
| 303.00 | 0.1963 | 0.0064 |
| 303.00 | 0.3062 | 0.0050 |
| 303.00 | 0.4062 | 0.0035 |
| 303.00 | 0.4898 | 0.0029 |
| 303.00 | 0.5973 | 0.0020 |
| 303.00 | 0.6708 | 0.0017 |
| 303.00 | 0.7388 | 0.0013 |
| 303.00 | 0.8012 | 0.0009 |
| 303.00 | 0.8562 | 0.0007 |
| 303.00 | 0.9031 | 0.0005 |
| 303.00 | 0.9601 | 0.0004 |
| 303.00 | 1.0000 | 0.0003 |
| 313.00 | 0.0000 | 0.0065 |
| 313.00 | 0.0989 | 0.0055 |
| 313.00 | 0.1963 | 0.0045 |
| 313.00 | 0.3062 | 0.0036 |
| 313.00 | 0.4062 | 0.0028 |
| 313.00 | 0.4898 | 0.0022 |
| 313.00 | 0.5973 | 0.0016 |
| 313.00 | 0.6708 | 0.0013 |
| 313.00 | 0.7388 | 0.0010 |
| 313.00 | 0.8012 | 0.0007 |
| 313.00 | 0.8562 | 0.0005 |
| 313.00 | 0.9031 | 0.0004 |
| 313.00 | 0.9601 | 0.0003 |
| 313.00 | 1.0000 | 0.0003 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanamine, N-ethyl- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.00 | 0.0000 | 0.0134 |
| 293.00 | 0.0989 | 0.0110 |
| 293.00 | 0.1963 | 0.0090 |
| 293.00 | 0.3062 | 0.0071 |
| 293.00 | 0.4062 | 0.0054 |
| 293.00 | 0.4898 | 0.0039 |
| 293.00 | 0.5973 | 0.0026 |
| 293.00 | 0.6708 | 0.0019 |
| 293.00 | 0.7388 | 0.0014 |
| 293.00 | 0.8012 | 0.0011 |
| 293.00 | 0.8562 | 0.0008 |
| 293.00 | 0.9031 | 0.0006 |
| 293.00 | 0.9601 | 0.0004 |
| 293.00 | 1.0000 | 0.0003 |
| 303.00 | 0.0000 | 0.0093 |
| 303.00 | 0.0989 | 0.0078 |
| 303.00 | 0.1963 | 0.0064 |
| 303.00 | 0.3062 | 0.0050 |
| 303.00 | 0.4062 | 0.0035 |
| 303.00 | 0.4898 | 0.0029 |
| 303.00 | 0.5973 | 0.0020 |
| 303.00 | 0.6708 | 0.0017 |
| 303.00 | 0.7388 | 0.0013 |
| 303.00 | 0.8012 | 0.0009 |
| 303.00 | 0.8562 | 0.0007 |
| 303.00 | 0.9031 | 0.0005 |
| 303.00 | 0.9601 | 0.0004 |
| 303.00 | 1.0000 | 0.0003 |
| 313.00 | 0.0000 | 0.0065 |
| 313.00 | 0.0989 | 0.0055 |
| 313.00 | 0.1963 | 0.0045 |
| 313.00 | 0.3062 | 0.0036 |
| 313.00 | 0.4062 | 0.0028 |
| 313.00 | 0.4898 | 0.0022 |
| 313.00 | 0.5973 | 0.0016 |
| 313.00 | 0.6708 | 0.0013 |
| 313.00 | 0.7388 | 0.0010 |
| 313.00 | 0.8012 | 0.0007 |
| 313.00 | 0.8562 | 0.0005 |
| 313.00 | 0.9031 | 0.0004 |
| 313.00 | 0.9601 | 0.0003 |
| 313.00 | 1.0000 | 0.0003 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanamine, N-ethyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.00 | 0.0000 | 830.1 |
| 293.00 | 0.0989 | 828.2 |
| 293.00 | 0.1963 | 824.8 |
| 293.00 | 0.3062 | 818.1 |
| 293.00 | 0.4062 | 814.4 |
| 293.00 | 0.4898 | 799.0 |
| 293.00 | 0.5973 | 795.6 |
| 293.00 | 0.6708 | 785.4 |
| 293.00 | 0.7388 | 779.4 |
| 293.00 | 0.8012 | 770.2 |
| 293.00 | 0.8562 | 759.5 |
| 293.00 | 0.9031 | 741.4 |
| 293.00 | 0.9601 | 720.7 |
| 293.00 | 1.0000 | 707.6 |
| 303.00 | 0.0000 | 822.1 |
| 303.00 | 0.0989 | 820.7 |
| 303.00 | 0.1963 | 814.6 |
| 303.00 | 0.3062 | 810.0 |
| 303.00 | 0.4062 | 808.4 |
| 303.00 | 0.4898 | 794.2 |
| 303.00 | 0.5973 | 790.7 |
| 303.00 | 0.6708 | 779.9 |
| 303.00 | 0.7388 | 773.3 |
| 303.00 | 0.8012 | 763.6 |
| 303.00 | 0.8562 | 753.7 |
| 303.00 | 0.9031 | 737.6 |
| 303.00 | 0.9601 | 709.2 |
| 303.00 | 1.0000 | 693.6 |
| 313.00 | 0.0000 | 815.7 |
| 313.00 | 0.0989 | 811.5 |
| 313.00 | 0.1963 | 806.3 |
| 313.00 | 0.3062 | 803.7 |
| 313.00 | 0.4062 | 802.1 |
| 313.00 | 0.4898 | 788.9 |
| 313.00 | 0.5973 | 782.9 |
| 313.00 | 0.6708 | 773.7 |
| 313.00 | 0.7388 | 769.7 |
| 313.00 | 0.8012 | 755.5 |
| 313.00 | 0.8562 | 745.6 |
| 313.00 | 0.9031 | 728.2 |
| 313.00 | 0.9601 | 694.8 |
| 313.00 | 1.0000 | 678.4 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanamine, N-ethyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.00 | 0.0000 | 830.1 |
| 293.00 | 0.0989 | 828.2 |
| 293.00 | 0.1963 | 824.8 |
| 293.00 | 0.3062 | 818.1 |
| 293.00 | 0.4062 | 814.4 |
| 293.00 | 0.4898 | 799.0 |
| 293.00 | 0.5973 | 795.6 |
| 293.00 | 0.6708 | 785.4 |
| 293.00 | 0.7388 | 779.4 |
| 293.00 | 0.8012 | 770.2 |
| 293.00 | 0.8562 | 759.5 |
| 293.00 | 0.9031 | 741.4 |
| 293.00 | 0.9601 | 720.7 |
| 293.00 | 1.0000 | 707.6 |
| 303.00 | 0.0000 | 822.1 |
| 303.00 | 0.0989 | 820.7 |
| 303.00 | 0.1963 | 814.6 |
| 303.00 | 0.3062 | 810.0 |
| 303.00 | 0.4062 | 808.4 |
| 303.00 | 0.4898 | 794.2 |
| 303.00 | 0.5973 | 790.7 |
| 303.00 | 0.6708 | 779.9 |
| 303.00 | 0.7388 | 773.3 |
| 303.00 | 0.8012 | 763.6 |
| 303.00 | 0.8562 | 753.7 |
| 303.00 | 0.9031 | 737.6 |
| 303.00 | 0.9601 | 709.2 |
| 303.00 | 1.0000 | 693.6 |
| 313.00 | 0.0000 | 815.7 |
| 313.00 | 0.0989 | 811.5 |
| 313.00 | 0.1963 | 806.3 |
| 313.00 | 0.3062 | 803.7 |
| 313.00 | 0.4062 | 802.1 |
| 313.00 | 0.4898 | 788.9 |
| 313.00 | 0.5973 | 782.9 |
| 313.00 | 0.6708 | 773.7 |
| 313.00 | 0.7388 | 769.7 |
| 313.00 | 0.8012 | 755.5 |
| 313.00 | 0.8562 | 745.6 |
| 313.00 | 0.9031 | 728.2 |
| 313.00 | 0.9601 | 694.8 |
| 313.00 | 1.0000 | 678.4 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanamine, N-ethyl- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.00 | 0.0000 | 1408.0 |
| 293.00 | 0.0989 | 1383.2 |
| 293.00 | 0.1963 | 1352.0 |
| 293.00 | 0.3062 | 1347.2 |
| 293.00 | 0.4062 | 1333.6 |
| 293.00 | 0.4898 | 1321.8 |
| 293.00 | 0.5973 | 1310.4 |
| 293.00 | 0.6708 | 1302.4 |
| 293.00 | 0.7388 | 1293.6 |
| 293.00 | 0.8012 | 1288.8 |
| 293.00 | 0.8562 | 1247.2 |
| 293.00 | 0.9031 | 1211.2 |
| 293.00 | 0.9601 | 1173.2 |
| 293.00 | 1.0000 | 1140.8 |
| 303.00 | 0.0000 | 1375.2 |
| 303.00 | 0.0989 | 1372.4 |
| 303.00 | 0.1963 | 1350.0 |
| 303.00 | 0.3062 | 1340.0 |
| 303.00 | 0.4062 | 1326.0 |
| 303.00 | 0.4898 | 1314.0 |
| 303.00 | 0.5973 | 1302.4 |
| 303.00 | 0.6708 | 1295.6 |
| 303.00 | 0.7388 | 1278.8 |
| 303.00 | 0.8012 | 1266.4 |
| 303.00 | 0.8562 | 1216.8 |
| 303.00 | 0.9031 | 1176.0 |
| 303.00 | 0.9601 | 1130.4 |
| 303.00 | 1.0000 | 1089.6 |
| 313.00 | 0.0000 | 1344.8 |
| 313.00 | 0.0989 | 1332.8 |
| 313.00 | 0.1963 | 1326.0 |
| 313.00 | 0.3062 | 1316.0 |
| 313.00 | 0.4062 | 1297.2 |
| 313.00 | 0.4898 | 1290.8 |
| 313.00 | 0.5973 | 1274.8 |
| 313.00 | 0.6708 | 1258.4 |
| 313.00 | 0.7388 | 1238.4 |
| 313.00 | 0.8012 | 1212.0 |
| 313.00 | 0.8562 | 1164.8 |
| 313.00 | 0.9031 | 1123.2 |
| 313.00 | 0.9601 | 1082.0 |
| 313.00 | 1.0000 | 1045.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanamine, N-ethyl- (1) - Liquid | Speed of sound, m/s - Liquid |
| 293.00 | 0.0000 | 1408.0 |
| 293.00 | 0.0989 | 1383.2 |
| 293.00 | 0.1963 | 1352.0 |
| 293.00 | 0.3062 | 1347.2 |
| 293.00 | 0.4062 | 1333.6 |
| 293.00 | 0.4898 | 1321.8 |
| 293.00 | 0.5973 | 1310.4 |
| 293.00 | 0.6708 | 1302.4 |
| 293.00 | 0.7388 | 1293.6 |
| 293.00 | 0.8012 | 1288.8 |
| 293.00 | 0.8562 | 1247.2 |
| 293.00 | 0.9031 | 1211.2 |
| 293.00 | 0.9601 | 1173.2 |
| 293.00 | 1.0000 | 1140.8 |
| 303.00 | 0.0000 | 1375.2 |
| 303.00 | 0.0989 | 1372.4 |
| 303.00 | 0.1963 | 1350.0 |
| 303.00 | 0.3062 | 1340.0 |
| 303.00 | 0.4062 | 1326.0 |
| 303.00 | 0.4898 | 1314.0 |
| 303.00 | 0.5973 | 1302.4 |
| 303.00 | 0.6708 | 1295.6 |
| 303.00 | 0.7388 | 1278.8 |
| 303.00 | 0.8012 | 1266.4 |
| 303.00 | 0.8562 | 1216.8 |
| 303.00 | 0.9031 | 1176.0 |
| 303.00 | 0.9601 | 1130.4 |
| 303.00 | 1.0000 | 1089.6 |
| 313.00 | 0.0000 | 1344.8 |
| 313.00 | 0.0989 | 1332.8 |
| 313.00 | 0.1963 | 1326.0 |
| 313.00 | 0.3062 | 1316.0 |
| 313.00 | 0.4062 | 1297.2 |
| 313.00 | 0.4898 | 1290.8 |
| 313.00 | 0.5973 | 1274.8 |
| 313.00 | 0.6708 | 1258.4 |
| 313.00 | 0.7388 | 1238.4 |
| 313.00 | 0.8012 | 1212.0 |
| 313.00 | 0.8562 | 1164.8 |
| 313.00 | 0.9031 | 1123.2 |
| 313.00 | 0.9601 | 1082.0 |
| 313.00 | 1.0000 | 1045.0 |