- Name
- 2,3-Butanediol
- InChI
- InChI=1S/C4H10O2/c1-3(5)4(2)6/h3-6H,1-2H3
- InChI Key
- OWBTYPJTUOEWEK-UHFFFAOYSA-N
- Formula
- C4H10O2
- SMILES
- CC(O)C(C)O
- Mol. Weight (g/mol)
- 90.12
- CAS
- 513-85-9
- 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
- Osmotic coefficient (2)
- η - Viscosity, Pa*s (2)
- Molar enthalpy (2)
- ρl - Mass density, kg/m3 (4)
- csound,fluid - Speed of Sound, m/s (2)
- Excess molar volume, m3/mol (2)
Osmotic coefficient [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Molality, mol/kg of 2,3-Butanediol (1) - Liquid | Osmotic coefficient - Liquid |
|---|---|
| 0.6071 | 0.9429 |
| 0.8087 | 0.9359 |
| 1.9946 | 0.9130 |
| 2.9601 | 0.9043 |
Osmotic coefficient [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Molality, mol/kg of 2,3-Butanediol (1) - Liquid | Osmotic coefficient - Liquid |
|---|---|
| 0.6071 | 0.9429 |
| 0.8087 | 0.9359 |
| 1.9946 | 0.9130 |
| 2.9601 | 0.9043 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0546 | 0.0419 |
| 298.15 | 0.1435 | 0.0367 |
| 298.15 | 0.2458 | 0.0305 |
| 298.15 | 0.3539 | 0.0240 |
| 298.15 | 0.4502 | 0.0186 |
| 298.15 | 0.4989 | 0.0161 |
| 298.15 | 0.5503 | 0.0135 |
| 298.15 | 0.6581 | 0.0089 |
| 298.15 | 0.7518 | 0.0058 |
| 298.15 | 0.8626 | 0.0033 |
| 298.15 | 0.9092 | 0.0025 |
| 298.15 | 0.9148 | 0.0024 |
| 298.15 | 0.9248 | 0.0022 |
| 298.15 | 0.9305 | 0.0021 |
| 298.15 | 0.9350 | 0.0020 |
| 298.15 | 0.9452 | 0.0019 |
| 298.15 | 0.9542 | 0.0017 |
| 298.15 | 0.9703 | 0.0015 |
| 298.15 | 0.9800 | 0.0013 |
| 298.15 | 0.9903 | 0.0011 |
| 298.15 | 0.9925 | 0.0010 |
| 298.15 | 0.9951 | 0.0010 |
| 308.15 | 0.0546 | 0.0216 |
| 308.15 | 0.1435 | 0.0191 |
| 308.15 | 0.2458 | 0.0161 |
| 308.15 | 0.3539 | 0.0130 |
| 308.15 | 0.4502 | 0.0103 |
| 308.15 | 0.4989 | 0.0091 |
| 308.15 | 0.5503 | 0.0078 |
| 308.15 | 0.6581 | 0.0054 |
| 308.15 | 0.7518 | 0.0038 |
| 308.15 | 0.8626 | 0.0023 |
| 308.15 | 0.9092 | 0.0017 |
| 308.15 | 0.9148 | 0.0017 |
| 308.15 | 0.9248 | 0.0016 |
| 308.15 | 0.9305 | 0.0015 |
| 308.15 | 0.9350 | 0.0015 |
| 308.15 | 0.9452 | 0.0014 |
| 308.15 | 0.9542 | 0.0013 |
| 308.15 | 0.9703 | 0.0011 |
| 308.15 | 0.9800 | 0.0010 |
| 308.15 | 0.9903 | 0.0008 |
| 308.15 | 0.9925 | 0.0008 |
| 308.15 | 0.9951 | 0.0008 |
| 318.15 | 0.0546 | 0.0120 |
| 318.15 | 0.1435 | 0.0106 |
| 318.15 | 0.2458 | 0.0090 |
| 318.15 | 0.3539 | 0.0072 |
| 318.15 | 0.4502 | 0.0057 |
| 318.15 | 0.4989 | 0.0050 |
| 318.15 | 0.5503 | 0.0043 |
| 318.15 | 0.6581 | 0.0030 |
| 318.15 | 0.7518 | 0.0022 |
| 318.15 | 0.8626 | 0.0014 |
| 318.15 | 0.9092 | 0.0011 |
| 318.15 | 0.9148 | 0.0011 |
| 318.15 | 0.9248 | 0.0010 |
| 318.15 | 0.9305 | 0.0010 |
| 318.15 | 0.9350 | 0.0010 |
| 318.15 | 0.9452 | 0.0009 |
| 318.15 | 0.9542 | 0.0009 |
| 318.15 | 0.9703 | 0.0008 |
| 318.15 | 0.9800 | 0.0007 |
| 318.15 | 0.9903 | 0.0007 |
| 318.15 | 0.9925 | 0.0006 |
| 318.15 | 0.9951 | 0.0006 |
| 328.15 | 0.0546 | 0.0073 |
| 328.15 | 0.1435 | 0.0064 |
| 328.15 | 0.2458 | 0.0054 |
| 328.15 | 0.3539 | 0.0044 |
| 328.15 | 0.4502 | 0.0035 |
| 328.15 | 0.4989 | 0.0031 |
| 328.15 | 0.5503 | 0.0027 |
| 328.15 | 0.6581 | 0.0019 |
| 328.15 | 0.7518 | 0.0014 |
| 328.15 | 0.8626 | 0.0010 |
| 328.15 | 0.9092 | 0.0008 |
| 328.15 | 0.9148 | 0.0008 |
| 328.15 | 0.9248 | 0.0008 |
| 328.15 | 0.9305 | 0.0007 |
| 328.15 | 0.9350 | 0.0007 |
| 328.15 | 0.9452 | 0.0007 |
| 328.15 | 0.9542 | 0.0007 |
| 328.15 | 0.9703 | 0.0006 |
| 328.15 | 0.9800 | 0.0006 |
| 328.15 | 0.9903 | 0.0005 |
| 328.15 | 0.9925 | 0.0005 |
| 328.15 | 0.9951 | 0.0005 |
| 338.15 | 0.0546 | 0.0049 |
| 338.15 | 0.1435 | 0.0044 |
| 338.15 | 0.2458 | 0.0037 |
| 338.15 | 0.3539 | 0.0031 |
| 338.15 | 0.4502 | 0.0025 |
| 338.15 | 0.4989 | 0.0022 |
| 338.15 | 0.5503 | 0.0020 |
| 338.15 | 0.6581 | 0.0014 |
| 338.15 | 0.7518 | 0.0011 |
| 338.15 | 0.8626 | 0.0008 |
| 338.15 | 0.9092 | 0.0007 |
| 338.15 | 0.9148 | 0.0006 |
| 338.15 | 0.9248 | 0.0006 |
| 338.15 | 0.9305 | 0.0006 |
| 338.15 | 0.9350 | 0.0006 |
| 338.15 | 0.9452 | 0.0006 |
| 338.15 | 0.9542 | 0.0006 |
| 338.15 | 0.9703 | 0.0005 |
| 338.15 | 0.9800 | 0.0005 |
| 338.15 | 0.9903 | 0.0005 |
| 338.15 | 0.9925 | 0.0005 |
| 338.15 | 0.9951 | 0.0005 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0546 | 0.0419 |
| 298.15 | 0.1435 | 0.0367 |
| 298.15 | 0.2458 | 0.0305 |
| 298.15 | 0.3539 | 0.0240 |
| 298.15 | 0.4502 | 0.0186 |
| 298.15 | 0.4989 | 0.0161 |
| 298.15 | 0.5503 | 0.0135 |
| 298.15 | 0.6581 | 0.0089 |
| 298.15 | 0.7518 | 0.0058 |
| 298.15 | 0.8626 | 0.0033 |
| 298.15 | 0.9092 | 0.0025 |
| 298.15 | 0.9148 | 0.0024 |
| 298.15 | 0.9248 | 0.0022 |
| 298.15 | 0.9305 | 0.0021 |
| 298.15 | 0.9350 | 0.0020 |
| 298.15 | 0.9452 | 0.0019 |
| 298.15 | 0.9542 | 0.0017 |
| 298.15 | 0.9703 | 0.0015 |
| 298.15 | 0.9800 | 0.0013 |
| 298.15 | 0.9903 | 0.0011 |
| 298.15 | 0.9925 | 0.0010 |
| 298.15 | 0.9951 | 0.0010 |
| 308.15 | 0.0546 | 0.0216 |
| 308.15 | 0.1435 | 0.0191 |
| 308.15 | 0.2458 | 0.0161 |
| 308.15 | 0.3539 | 0.0130 |
| 308.15 | 0.4502 | 0.0103 |
| 308.15 | 0.4989 | 0.0091 |
| 308.15 | 0.5503 | 0.0078 |
| 308.15 | 0.6581 | 0.0054 |
| 308.15 | 0.7518 | 0.0038 |
| 308.15 | 0.8626 | 0.0023 |
| 308.15 | 0.9092 | 0.0017 |
| 308.15 | 0.9148 | 0.0017 |
| 308.15 | 0.9248 | 0.0016 |
| 308.15 | 0.9305 | 0.0015 |
| 308.15 | 0.9350 | 0.0015 |
| 308.15 | 0.9452 | 0.0014 |
| 308.15 | 0.9542 | 0.0013 |
| 308.15 | 0.9703 | 0.0011 |
| 308.15 | 0.9800 | 0.0010 |
| 308.15 | 0.9903 | 0.0008 |
| 308.15 | 0.9925 | 0.0008 |
| 308.15 | 0.9951 | 0.0008 |
| 318.15 | 0.0546 | 0.0120 |
| 318.15 | 0.1435 | 0.0106 |
| 318.15 | 0.2458 | 0.0090 |
| 318.15 | 0.3539 | 0.0072 |
| 318.15 | 0.4502 | 0.0057 |
| 318.15 | 0.4989 | 0.0050 |
| 318.15 | 0.5503 | 0.0043 |
| 318.15 | 0.6581 | 0.0030 |
| 318.15 | 0.7518 | 0.0022 |
| 318.15 | 0.8626 | 0.0014 |
| 318.15 | 0.9092 | 0.0011 |
| 318.15 | 0.9148 | 0.0011 |
| 318.15 | 0.9248 | 0.0010 |
| 318.15 | 0.9305 | 0.0010 |
| 318.15 | 0.9350 | 0.0010 |
| 318.15 | 0.9452 | 0.0009 |
| 318.15 | 0.9542 | 0.0009 |
| 318.15 | 0.9703 | 0.0008 |
| 318.15 | 0.9800 | 0.0007 |
| 318.15 | 0.9903 | 0.0007 |
| 318.15 | 0.9925 | 0.0006 |
| 318.15 | 0.9951 | 0.0006 |
| 328.15 | 0.0546 | 0.0073 |
| 328.15 | 0.1435 | 0.0064 |
| 328.15 | 0.2458 | 0.0054 |
| 328.15 | 0.3539 | 0.0044 |
| 328.15 | 0.4502 | 0.0035 |
| 328.15 | 0.4989 | 0.0031 |
| 328.15 | 0.5503 | 0.0027 |
| 328.15 | 0.6581 | 0.0019 |
| 328.15 | 0.7518 | 0.0014 |
| 328.15 | 0.8626 | 0.0010 |
| 328.15 | 0.9092 | 0.0008 |
| 328.15 | 0.9148 | 0.0008 |
| 328.15 | 0.9248 | 0.0008 |
| 328.15 | 0.9305 | 0.0007 |
| 328.15 | 0.9350 | 0.0007 |
| 328.15 | 0.9452 | 0.0007 |
| 328.15 | 0.9542 | 0.0007 |
| 328.15 | 0.9703 | 0.0006 |
| 328.15 | 0.9800 | 0.0006 |
| 328.15 | 0.9903 | 0.0005 |
| 328.15 | 0.9925 | 0.0005 |
| 328.15 | 0.9951 | 0.0005 |
| 338.15 | 0.0546 | 0.0049 |
| 338.15 | 0.1435 | 0.0044 |
| 338.15 | 0.2458 | 0.0037 |
| 338.15 | 0.3539 | 0.0031 |
| 338.15 | 0.4502 | 0.0025 |
| 338.15 | 0.4989 | 0.0022 |
| 338.15 | 0.5503 | 0.0020 |
| 338.15 | 0.6581 | 0.0014 |
| 338.15 | 0.7518 | 0.0011 |
| 338.15 | 0.8626 | 0.0008 |
| 338.15 | 0.9092 | 0.0007 |
| 338.15 | 0.9148 | 0.0006 |
| 338.15 | 0.9248 | 0.0006 |
| 338.15 | 0.9305 | 0.0006 |
| 338.15 | 0.9350 | 0.0006 |
| 338.15 | 0.9452 | 0.0006 |
| 338.15 | 0.9542 | 0.0006 |
| 338.15 | 0.9703 | 0.0005 |
| 338.15 | 0.9800 | 0.0005 |
| 338.15 | 0.9903 | 0.0005 |
| 338.15 | 0.9925 | 0.0005 |
| 338.15 | 0.9951 | 0.0005 |
Molar enthalpy of dilution, kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Initial molality of solute, mol/kg - Liquid | Final molality of solute, mol/kg - Liquid | Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.2858 | 0.1381 | -0.0971 |
| 0.5103 | 0.2441 | -0.1585 |
| 0.5972 | 0.2846 | -0.2086 |
| 0.6375 | 0.3032 | -0.2330 |
| 0.7085 | 0.3359 | -0.2512 |
| 0.7651 | 0.3619 | -0.2685 |
| 0.8388 | 0.3954 | -0.3022 |
| 1.2251 | 0.5678 | -0.4852 |
| 1.5591 | 0.7123 | -0.6443 |
| 2.0031 | 0.8980 | -0.8416 |
| 3.2549 | 1.3861 | -1.4294 |
| 3.3033 | 1.404 | -1.4497 |
| 3.7334 | 1.56 | -1.7478 |
| 4.2572 | 1.743 | -1.905 |
Molar enthalpy of dilution, kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Initial molality of solute, mol/kg - Liquid | Final molality of solute, mol/kg - Liquid | Molar enthalpy of dilution, kJ/mol - Liquid |
| 0.2858 | 0.1381 | -0.0971 |
| 0.5103 | 0.2441 | -0.1585 |
| 0.5972 | 0.2846 | -0.2086 |
| 0.6375 | 0.3032 | -0.2330 |
| 0.7085 | 0.3359 | -0.2512 |
| 0.7651 | 0.3619 | -0.2685 |
| 0.8388 | 0.3954 | -0.3022 |
| 1.2251 | 0.5678 | -0.4852 |
| 1.5591 | 0.7123 | -0.6443 |
| 2.0031 | 0.8980 | -0.8416 |
| 3.2549 | 1.3861 | -1.4294 |
| 3.3033 | 1.404 | -1.4497 |
| 3.7334 | 1.56 | -1.7478 |
| 4.2572 | 1.743 | -1.905 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 2,3-Butanediol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0618 | 1014.1 |
| 0.1379 | 1021.5 |
| 0.1796 | 1023.1 |
| 0.2179 | 1023.2 |
| 0.2417 | 1022.7 |
| 0.2696 | 1022.0 |
| 0.3027 | 1021.0 |
| 0.3426 | 1019.5 |
| 0.3913 | 1017.6 |
| 0.4524 | 1015.2 |
| 0.5308 | 1012.2 |
| 0.6352 | 1008.4 |
| 0.7805 | 1004.1 |
| 0.9001 | 1000.9 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0546 | 999.76 |
| 298.15 | 0.1435 | 1001.87 |
| 298.15 | 0.2458 | 1004.58 |
| 298.15 | 0.3539 | 1007.87 |
| 298.15 | 0.4502 | 1011.19 |
| 298.15 | 0.4989 | 1013.01 |
| 298.15 | 0.5503 | 1014.99 |
| 298.15 | 0.6581 | 1019.13 |
| 298.15 | 0.7518 | 1021.95 |
| 298.15 | 0.8626 | 1021.36 |
| 298.15 | 0.9092 | 1017.89 |
| 298.15 | 0.9148 | 1017.25 |
| 298.15 | 0.9248 | 1015.95 |
| 298.15 | 0.9305 | 1015.11 |
| 298.15 | 0.9350 | 1014.4 |
| 298.15 | 0.9452 | 1012.61 |
| 298.15 | 0.9542 | 1010.78 |
| 298.15 | 0.9703 | 1006.89 |
| 298.15 | 0.9800 | 1004.1 |
| 298.15 | 0.9903 | 1000.7 |
| 298.15 | 0.9925 | 999.91 |
| 298.15 | 0.9951 | 998.95 |
| 308.15 | 0.0546 | 993.26 |
| 308.15 | 0.1435 | 995.29 |
| 308.15 | 0.2458 | 997.92 |
| 308.15 | 0.3539 | 1001.1 |
| 308.15 | 0.4502 | 1004.34 |
| 308.15 | 0.4989 | 1006.11 |
| 308.15 | 0.5503 | 1008.06 |
| 308.15 | 0.6581 | 1012.2 |
| 308.15 | 0.7518 | 1015.17 |
| 308.15 | 0.8626 | 1015.24 |
| 308.15 | 0.9092 | 1012.39 |
| 308.15 | 0.9148 | 1011.85 |
| 308.15 | 0.9248 | 1010.74 |
| 308.15 | 0.9305 | 1010.02 |
| 308.15 | 0.9350 | 1009.4 |
| 308.15 | 0.9452 | 1007.83 |
| 308.15 | 0.9542 | 1006.24 |
| 308.15 | 0.9703 | 1002.81 |
| 308.15 | 0.9800 | 1000.33 |
| 308.15 | 0.9903 | 997.3 |
| 308.15 | 0.9925 | 996.59 |
| 308.15 | 0.9951 | 995.73 |
| 318.15 | 0.0546 | 985.33 |
| 318.15 | 0.1435 | 987.34 |
| 318.15 | 0.2458 | 989.9 |
| 318.15 | 0.3539 | 993.04 |
| 318.15 | 0.4502 | 996.28 |
| 318.15 | 0.4989 | 998.08 |
| 318.15 | 0.5503 | 1000.07 |
| 318.15 | 0.6581 | 1004.28 |
| 318.15 | 0.7518 | 1007.26 |
| 318.15 | 0.8626 | 1007.49 |
| 318.15 | 0.9092 | 1005.07 |
| 318.15 | 0.9148 | 1004.61 |
| 318.15 | 0.9248 | 1003.67 |
| 318.15 | 0.9305 | 1003.07 |
| 318.15 | 0.9350 | 1002.56 |
| 318.15 | 0.9452 | 1001.27 |
| 318.15 | 0.9542 | 999.96 |
| 318.15 | 0.9703 | 997.18 |
| 318.15 | 0.9800 | 995.19 |
| 318.15 | 0.9903 | 992.79 |
| 318.15 | 0.9925 | 992.23 |
| 318.15 | 0.9951 | 991.55 |
| 328.15 | 0.0546 | 971.78 |
| 328.15 | 0.1435 | 973.84 |
| 328.15 | 0.2458 | 976.48 |
| 328.15 | 0.3539 | 979.73 |
| 328.15 | 0.4502 | 983.14 |
| 328.15 | 0.4989 | 985.04 |
| 328.15 | 0.5503 | 987.17 |
| 328.15 | 0.6581 | 991.86 |
| 328.15 | 0.7518 | 995.6 |
| 328.15 | 0.8626 | 997.57 |
| 328.15 | 0.9092 | 996.39 |
| 328.15 | 0.9148 | 996.11 |
| 328.15 | 0.9248 | 995.52 |
| 328.15 | 0.9305 | 995.13 |
| 328.15 | 0.9350 | 994.78 |
| 328.15 | 0.9452 | 993.9 |
| 328.15 | 0.9542 | 992.98 |
| 328.15 | 0.9703 | 990.96 |
| 328.15 | 0.9800 | 989.48 |
| 328.15 | 0.9903 | 987.67 |
| 328.15 | 0.9925 | 987.24 |
| 328.15 | 0.9951 | 986.72 |
| 338.15 | 0.0546 | 963.14 |
| 338.15 | 0.1435 | 965.14 |
| 338.15 | 0.2458 | 967.72 |
| 338.15 | 0.3539 | 970.91 |
| 338.15 | 0.4502 | 974.25 |
| 338.15 | 0.4989 | 976.14 |
| 338.15 | 0.5503 | 978.26 |
| 338.15 | 0.6581 | 982.97 |
| 338.15 | 0.7518 | 986.9 |
| 338.15 | 0.8626 | 989.57 |
| 338.15 | 0.9092 | 988.99 |
| 338.15 | 0.9148 | 988.8 |
| 338.15 | 0.9248 | 988.39 |
| 338.15 | 0.9305 | 988.1 |
| 338.15 | 0.9350 | 987.85 |
| 338.15 | 0.9452 | 987.18 |
| 338.15 | 0.9542 | 986.46 |
| 338.15 | 0.9703 | 984.86 |
| 338.15 | 0.9800 | 983.67 |
| 338.15 | 0.9903 | 982.18 |
| 338.15 | 0.9925 | 981.83 |
| 338.15 | 0.9951 | 981.4 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 2,3-Butanediol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0618 | 1014.1 |
| 0.1379 | 1021.5 |
| 0.1796 | 1023.1 |
| 0.2179 | 1023.2 |
| 0.2417 | 1022.7 |
| 0.2696 | 1022.0 |
| 0.3027 | 1021.0 |
| 0.3426 | 1019.5 |
| 0.3913 | 1017.6 |
| 0.4524 | 1015.2 |
| 0.5308 | 1012.2 |
| 0.6352 | 1008.4 |
| 0.7805 | 1004.1 |
| 0.9001 | 1000.9 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0546 | 999.76 |
| 298.15 | 0.1435 | 1001.87 |
| 298.15 | 0.2458 | 1004.58 |
| 298.15 | 0.3539 | 1007.87 |
| 298.15 | 0.4502 | 1011.19 |
| 298.15 | 0.4989 | 1013.01 |
| 298.15 | 0.5503 | 1014.99 |
| 298.15 | 0.6581 | 1019.13 |
| 298.15 | 0.7518 | 1021.95 |
| 298.15 | 0.8626 | 1021.36 |
| 298.15 | 0.9092 | 1017.89 |
| 298.15 | 0.9148 | 1017.25 |
| 298.15 | 0.9248 | 1015.95 |
| 298.15 | 0.9305 | 1015.11 |
| 298.15 | 0.9350 | 1014.4 |
| 298.15 | 0.9452 | 1012.61 |
| 298.15 | 0.9542 | 1010.78 |
| 298.15 | 0.9703 | 1006.89 |
| 298.15 | 0.9800 | 1004.1 |
| 298.15 | 0.9903 | 1000.7 |
| 298.15 | 0.9925 | 999.91 |
| 298.15 | 0.9951 | 998.95 |
| 308.15 | 0.0546 | 993.26 |
| 308.15 | 0.1435 | 995.29 |
| 308.15 | 0.2458 | 997.92 |
| 308.15 | 0.3539 | 1001.1 |
| 308.15 | 0.4502 | 1004.34 |
| 308.15 | 0.4989 | 1006.11 |
| 308.15 | 0.5503 | 1008.06 |
| 308.15 | 0.6581 | 1012.2 |
| 308.15 | 0.7518 | 1015.17 |
| 308.15 | 0.8626 | 1015.24 |
| 308.15 | 0.9092 | 1012.39 |
| 308.15 | 0.9148 | 1011.85 |
| 308.15 | 0.9248 | 1010.74 |
| 308.15 | 0.9305 | 1010.02 |
| 308.15 | 0.9350 | 1009.4 |
| 308.15 | 0.9452 | 1007.83 |
| 308.15 | 0.9542 | 1006.24 |
| 308.15 | 0.9703 | 1002.81 |
| 308.15 | 0.9800 | 1000.33 |
| 308.15 | 0.9903 | 997.3 |
| 308.15 | 0.9925 | 996.59 |
| 308.15 | 0.9951 | 995.73 |
| 318.15 | 0.0546 | 985.33 |
| 318.15 | 0.1435 | 987.34 |
| 318.15 | 0.2458 | 989.9 |
| 318.15 | 0.3539 | 993.04 |
| 318.15 | 0.4502 | 996.28 |
| 318.15 | 0.4989 | 998.08 |
| 318.15 | 0.5503 | 1000.07 |
| 318.15 | 0.6581 | 1004.28 |
| 318.15 | 0.7518 | 1007.26 |
| 318.15 | 0.8626 | 1007.49 |
| 318.15 | 0.9092 | 1005.07 |
| 318.15 | 0.9148 | 1004.61 |
| 318.15 | 0.9248 | 1003.67 |
| 318.15 | 0.9305 | 1003.07 |
| 318.15 | 0.9350 | 1002.56 |
| 318.15 | 0.9452 | 1001.27 |
| 318.15 | 0.9542 | 999.96 |
| 318.15 | 0.9703 | 997.18 |
| 318.15 | 0.9800 | 995.19 |
| 318.15 | 0.9903 | 992.79 |
| 318.15 | 0.9925 | 992.23 |
| 318.15 | 0.9951 | 991.55 |
| 328.15 | 0.0546 | 971.78 |
| 328.15 | 0.1435 | 973.84 |
| 328.15 | 0.2458 | 976.48 |
| 328.15 | 0.3539 | 979.73 |
| 328.15 | 0.4502 | 983.14 |
| 328.15 | 0.4989 | 985.04 |
| 328.15 | 0.5503 | 987.17 |
| 328.15 | 0.6581 | 991.86 |
| 328.15 | 0.7518 | 995.6 |
| 328.15 | 0.8626 | 997.57 |
| 328.15 | 0.9092 | 996.39 |
| 328.15 | 0.9148 | 996.11 |
| 328.15 | 0.9248 | 995.52 |
| 328.15 | 0.9305 | 995.13 |
| 328.15 | 0.9350 | 994.78 |
| 328.15 | 0.9452 | 993.9 |
| 328.15 | 0.9542 | 992.98 |
| 328.15 | 0.9703 | 990.96 |
| 328.15 | 0.9800 | 989.48 |
| 328.15 | 0.9903 | 987.67 |
| 328.15 | 0.9925 | 987.24 |
| 328.15 | 0.9951 | 986.72 |
| 338.15 | 0.0546 | 963.14 |
| 338.15 | 0.1435 | 965.14 |
| 338.15 | 0.2458 | 967.72 |
| 338.15 | 0.3539 | 970.91 |
| 338.15 | 0.4502 | 974.25 |
| 338.15 | 0.4989 | 976.14 |
| 338.15 | 0.5503 | 978.26 |
| 338.15 | 0.6581 | 982.97 |
| 338.15 | 0.7518 | 986.9 |
| 338.15 | 0.8626 | 989.57 |
| 338.15 | 0.9092 | 988.99 |
| 338.15 | 0.9148 | 988.8 |
| 338.15 | 0.9248 | 988.39 |
| 338.15 | 0.9305 | 988.1 |
| 338.15 | 0.9350 | 987.85 |
| 338.15 | 0.9452 | 987.18 |
| 338.15 | 0.9542 | 986.46 |
| 338.15 | 0.9703 | 984.86 |
| 338.15 | 0.9800 | 983.67 |
| 338.15 | 0.9903 | 982.18 |
| 338.15 | 0.9925 | 981.83 |
| 338.15 | 0.9951 | 981.4 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0546 | 1483.0 |
| 298.15 | 0.1435 | 1501.3 |
| 298.15 | 0.2458 | 1520.7 |
| 298.15 | 0.3539 | 1548.5 |
| 298.15 | 0.4502 | 1576.9 |
| 298.15 | 0.4989 | 1589.5 |
| 298.15 | 0.5503 | 1604.9 |
| 298.15 | 0.6581 | 1637.2 |
| 298.15 | 0.7518 | 1667.8 |
| 298.15 | 0.8626 | 1673.2 |
| 298.15 | 0.9092 | 1657.9 |
| 298.15 | 0.9148 | 1651.5 |
| 298.15 | 0.9248 | 1645.4 |
| 298.15 | 0.9305 | 1640.3 |
| 298.15 | 0.9350 | 1637.1 |
| 298.15 | 0.9452 | 1628.0 |
| 298.15 | 0.9542 | 1616.9 |
| 298.15 | 0.9703 | 1610.2 |
| 298.15 | 0.9800 | 1596.8 |
| 298.15 | 0.9903 | 1586.3 |
| 298.15 | 0.9925 | 1582.5 |
| 298.15 | 0.9951 | 1577.9 |
| 308.15 | 0.0546 | 1446.8 |
| 308.15 | 0.1435 | 1464.7 |
| 308.15 | 0.2458 | 1483.6 |
| 308.15 | 0.3539 | 1510.7 |
| 308.15 | 0.4502 | 1538.4 |
| 308.15 | 0.4989 | 1550.7 |
| 308.15 | 0.5503 | 1565.8 |
| 308.15 | 0.6581 | 1597.3 |
| 308.15 | 0.7518 | 1627.1 |
| 308.15 | 0.8626 | 1632.4 |
| 308.15 | 0.9092 | 1617.5 |
| 308.15 | 0.9148 | 1611.2 |
| 308.15 | 0.9248 | 1605.3 |
| 308.15 | 0.9305 | 1600.3 |
| 308.15 | 0.9350 | 1597.2 |
| 308.15 | 0.9452 | 1588.3 |
| 308.15 | 0.9542 | 1577.5 |
| 308.15 | 0.9703 | 1570.9 |
| 308.15 | 0.9800 | 1557.9 |
| 308.15 | 0.9903 | 1547.6 |
| 308.15 | 0.9925 | 1543.9 |
| 308.15 | 0.9951 | 1539.4 |
| 318.15 | 0.0546 | 1418.4 |
| 318.15 | 0.1435 | 1436.0 |
| 318.15 | 0.2458 | 1454.5 |
| 318.15 | 0.3539 | 1481.1 |
| 318.15 | 0.4502 | 1508.2 |
| 318.15 | 0.4989 | 1520.3 |
| 318.15 | 0.5503 | 1535.1 |
| 318.15 | 0.6581 | 1566.0 |
| 318.15 | 0.7518 | 1595.2 |
| 318.15 | 0.8626 | 1605.3 |
| 318.15 | 0.9092 | 1598.9 |
| 318.15 | 0.9148 | 1596.7 |
| 318.15 | 0.9248 | 1596.3 |
| 318.15 | 0.9305 | 1590.4 |
| 318.15 | 0.9350 | 1583.1 |
| 318.15 | 0.9452 | 1580.2 |
| 318.15 | 0.9542 | 1578.1 |
| 318.15 | 0.9703 | 1571.6 |
| 318.15 | 0.9800 | 1558.5 |
| 318.15 | 0.9903 | 1548.2 |
| 318.15 | 0.9925 | 1544.5 |
| 318.15 | 0.9951 | 1540.0 |
| 328.15 | 0.0546 | 1397.7 |
| 328.15 | 0.1435 | 1413.9 |
| 328.15 | 0.2458 | 1431.2 |
| 328.15 | 0.3539 | 1456.9 |
| 328.15 | 0.4502 | 1482.2 |
| 328.15 | 0.4989 | 1494.1 |
| 328.15 | 0.5503 | 1508.7 |
| 328.15 | 0.6581 | 1537.6 |
| 328.15 | 0.7518 | 1567.1 |
| 328.15 | 0.8626 | 1596.6 |
| 328.15 | 0.9092 | 1594.5 |
| 328.15 | 0.9148 | 1592.9 |
| 328.15 | 0.9248 | 1590.3 |
| 328.15 | 0.9305 | 1585.9 |
| 328.15 | 0.9350 | 1570.1 |
| 328.15 | 0.9452 | 1574.2 |
| 328.15 | 0.9542 | 1573.0 |
| 328.15 | 0.9703 | 1570.4 |
| 328.15 | 0.9800 | 1561.6 |
| 328.15 | 0.9903 | 1553.7 |
| 328.15 | 0.9925 | 1551.3 |
| 328.15 | 0.9951 | 1548.3 |
| 338.15 | 0.0546 | 1379.0 |
| 338.15 | 0.1435 | 1394.6 |
| 338.15 | 0.2458 | 1410.6 |
| 338.15 | 0.3539 | 1433.2 |
| 338.15 | 0.4502 | 1457.5 |
| 338.15 | 0.4989 | 1468.9 |
| 338.15 | 0.5503 | 1482.2 |
| 338.15 | 0.6581 | 1510.5 |
| 338.15 | 0.7518 | 1540.0 |
| 338.15 | 0.8626 | 1573.7 |
| 338.15 | 0.9092 | 1577.3 |
| 338.15 | 0.9148 | 1576.0 |
| 338.15 | 0.9248 | 1576.1 |
| 338.15 | 0.9305 | 1572.2 |
| 338.15 | 0.9350 | 1559.7 |
| 338.15 | 0.9452 | 1564.6 |
| 338.15 | 0.9542 | 1566.2 |
| 338.15 | 0.9703 | 1566.1 |
| 338.15 | 0.9800 | 1561.3 |
| 338.15 | 0.9903 | 1556.6 |
| 338.15 | 0.9925 | 1555.4 |
| 338.15 | 0.9951 | 1552.7 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Water (2) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0546 | 1483.0 |
| 298.15 | 0.1435 | 1501.3 |
| 298.15 | 0.2458 | 1520.7 |
| 298.15 | 0.3539 | 1548.5 |
| 298.15 | 0.4502 | 1576.9 |
| 298.15 | 0.4989 | 1589.5 |
| 298.15 | 0.5503 | 1604.9 |
| 298.15 | 0.6581 | 1637.2 |
| 298.15 | 0.7518 | 1667.8 |
| 298.15 | 0.8626 | 1673.2 |
| 298.15 | 0.9092 | 1657.9 |
| 298.15 | 0.9148 | 1651.5 |
| 298.15 | 0.9248 | 1645.4 |
| 298.15 | 0.9305 | 1640.3 |
| 298.15 | 0.9350 | 1637.1 |
| 298.15 | 0.9452 | 1628.0 |
| 298.15 | 0.9542 | 1616.9 |
| 298.15 | 0.9703 | 1610.2 |
| 298.15 | 0.9800 | 1596.8 |
| 298.15 | 0.9903 | 1586.3 |
| 298.15 | 0.9925 | 1582.5 |
| 298.15 | 0.9951 | 1577.9 |
| 308.15 | 0.0546 | 1446.8 |
| 308.15 | 0.1435 | 1464.7 |
| 308.15 | 0.2458 | 1483.6 |
| 308.15 | 0.3539 | 1510.7 |
| 308.15 | 0.4502 | 1538.4 |
| 308.15 | 0.4989 | 1550.7 |
| 308.15 | 0.5503 | 1565.8 |
| 308.15 | 0.6581 | 1597.3 |
| 308.15 | 0.7518 | 1627.1 |
| 308.15 | 0.8626 | 1632.4 |
| 308.15 | 0.9092 | 1617.5 |
| 308.15 | 0.9148 | 1611.2 |
| 308.15 | 0.9248 | 1605.3 |
| 308.15 | 0.9305 | 1600.3 |
| 308.15 | 0.9350 | 1597.2 |
| 308.15 | 0.9452 | 1588.3 |
| 308.15 | 0.9542 | 1577.5 |
| 308.15 | 0.9703 | 1570.9 |
| 308.15 | 0.9800 | 1557.9 |
| 308.15 | 0.9903 | 1547.6 |
| 308.15 | 0.9925 | 1543.9 |
| 308.15 | 0.9951 | 1539.4 |
| 318.15 | 0.0546 | 1418.4 |
| 318.15 | 0.1435 | 1436.0 |
| 318.15 | 0.2458 | 1454.5 |
| 318.15 | 0.3539 | 1481.1 |
| 318.15 | 0.4502 | 1508.2 |
| 318.15 | 0.4989 | 1520.3 |
| 318.15 | 0.5503 | 1535.1 |
| 318.15 | 0.6581 | 1566.0 |
| 318.15 | 0.7518 | 1595.2 |
| 318.15 | 0.8626 | 1605.3 |
| 318.15 | 0.9092 | 1598.9 |
| 318.15 | 0.9148 | 1596.7 |
| 318.15 | 0.9248 | 1596.3 |
| 318.15 | 0.9305 | 1590.4 |
| 318.15 | 0.9350 | 1583.1 |
| 318.15 | 0.9452 | 1580.2 |
| 318.15 | 0.9542 | 1578.1 |
| 318.15 | 0.9703 | 1571.6 |
| 318.15 | 0.9800 | 1558.5 |
| 318.15 | 0.9903 | 1548.2 |
| 318.15 | 0.9925 | 1544.5 |
| 318.15 | 0.9951 | 1540.0 |
| 328.15 | 0.0546 | 1397.7 |
| 328.15 | 0.1435 | 1413.9 |
| 328.15 | 0.2458 | 1431.2 |
| 328.15 | 0.3539 | 1456.9 |
| 328.15 | 0.4502 | 1482.2 |
| 328.15 | 0.4989 | 1494.1 |
| 328.15 | 0.5503 | 1508.7 |
| 328.15 | 0.6581 | 1537.6 |
| 328.15 | 0.7518 | 1567.1 |
| 328.15 | 0.8626 | 1596.6 |
| 328.15 | 0.9092 | 1594.5 |
| 328.15 | 0.9148 | 1592.9 |
| 328.15 | 0.9248 | 1590.3 |
| 328.15 | 0.9305 | 1585.9 |
| 328.15 | 0.9350 | 1570.1 |
| 328.15 | 0.9452 | 1574.2 |
| 328.15 | 0.9542 | 1573.0 |
| 328.15 | 0.9703 | 1570.4 |
| 328.15 | 0.9800 | 1561.6 |
| 328.15 | 0.9903 | 1553.7 |
| 328.15 | 0.9925 | 1551.3 |
| 328.15 | 0.9951 | 1548.3 |
| 338.15 | 0.0546 | 1379.0 |
| 338.15 | 0.1435 | 1394.6 |
| 338.15 | 0.2458 | 1410.6 |
| 338.15 | 0.3539 | 1433.2 |
| 338.15 | 0.4502 | 1457.5 |
| 338.15 | 0.4989 | 1468.9 |
| 338.15 | 0.5503 | 1482.2 |
| 338.15 | 0.6581 | 1510.5 |
| 338.15 | 0.7518 | 1540.0 |
| 338.15 | 0.8626 | 1573.7 |
| 338.15 | 0.9092 | 1577.3 |
| 338.15 | 0.9148 | 1576.0 |
| 338.15 | 0.9248 | 1576.1 |
| 338.15 | 0.9305 | 1572.2 |
| 338.15 | 0.9350 | 1559.7 |
| 338.15 | 0.9452 | 1564.6 |
| 338.15 | 0.9542 | 1566.2 |
| 338.15 | 0.9703 | 1566.1 |
| 338.15 | 0.9800 | 1561.3 |
| 338.15 | 0.9903 | 1556.6 |
| 338.15 | 0.9925 | 1555.4 |
| 338.15 | 0.9951 | 1552.7 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 2,3-Butanediol (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0618 | -3.7100e-07 |
| 0.1379 | -6.5310e-07 |
| 0.1796 | -7.6690e-07 |
| 0.2179 | -8.3460e-07 |
| 0.2417 | -8.5890e-07 |
| 0.2696 | -8.7860e-07 |
| 0.3027 | -8.9540e-07 |
| 0.3426 | -8.9640e-07 |
| 0.3913 | -8.8220e-07 |
| 0.4524 | -8.4550e-07 |
| 0.5308 | -7.7320e-07 |
| 0.6352 | -6.3430e-07 |
| 0.7805 | -4.1560e-07 |
| 0.9001 | -1.9250e-07 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 2,3-Butanediol (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0618 | -3.7100e-07 |
| 0.1379 | -6.5310e-07 |
| 0.1796 | -7.6690e-07 |
| 0.2179 | -8.3460e-07 |
| 0.2417 | -8.5890e-07 |
| 0.2696 | -8.7860e-07 |
| 0.3027 | -8.9540e-07 |
| 0.3426 | -8.9640e-07 |
| 0.3913 | -8.8220e-07 |
| 0.4524 | -8.4550e-07 |
| 0.5308 | -7.7320e-07 |
| 0.6352 | -6.3430e-07 |
| 0.7805 | -4.1560e-07 |
| 0.9001 | -1.9250e-07 |
Sources
- Isopiestic determination of osmotic and activity coefficients of aqueous solutions of aliphatic polyols at 298.15K
- Experimental study of the excess molar volume of ternary mixtures containing {water + (1,2-propanediol, or 1,3-propanediol, or 1,2-butanediol, or 1,3-butanediol, or 1,4-butanediol, or 2,3-butanediol) + electrolytes} at a temperature of 298.15 K and atmospheric pressure
- Enthalpies of dilution of aqueous solutions of n-butanol, butanediols, 1,2,4-butanetriol, and 1,2,3,4-butanetetrol at 298.15K
- Densities, Dynamic Viscosities, Speeds of Sound, and Relative Permittivities for Water + Alkanediols (Propane-1,2- and -1,3-diol and Butane-1,2-, -1,3-, -1,4-, and -2,3-Diol) at Different Temperatures