- Name
- Ethanol, 2-butoxy-
- InChI
- InChI=1S/C6H14O2/c1-2-3-5-8-6-4-7/h7H,2-6H2,1H3
- InChI Key
- POAOYUHQDCAZBD-UHFFFAOYSA-N
- Formula
- C6H14O2
- SMILES
- CCCCOCCO
- Mol. Weight (g/mol)
- 118.17
- CAS
- 111-76-2
- 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 (3)
- η - Viscosity, Pa*s (4)
- εr - Relative permittivity at zero frequency
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (6)
- csound,fluid - Speed of Sound, m/s
- λ - Thermal conductivity, W/m/K
Mass fraction of Ethanol, 2-butoxy- (1) [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass fraction of Ethanol, 2-butoxy- (1) - Liquid mixture 1 |
|---|---|
| 323.15 | 0.1880 |
| 328.15 | 0.1360 |
| 333.15 | 0.1180 |
| 343.15 | 0.1020 |
| 353.15 | 0.0960 |
| 363.15 | 0.0988 |
| 373.15 | 0.1040 |
| 383.15 | 0.1200 |
| 393.15 | 0.1460 |
| 401.15 | 0.2130 |
Mass fraction of Ethanol, 2-butoxy- (1) [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mass fraction of Ethanol, 2-butoxy- (1) - Liquid mixture 2 |
|---|---|
| 323.15 | 0.4160 |
| 328.15 | 0.5000 |
| 333.15 | 0.5410 |
| 343.15 | 0.5830 |
| 353.15 | 0.6000 |
| 363.15 | 0.6030 |
| 373.15 | 0.5960 |
| 383.15 | 0.5730 |
| 393.15 | 0.5400 |
| 401.15 | 0.4460 |
Henry's Law constant (molality scale), kPa*kg/mol of Ethanol, 2-butoxy- (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of Ethanol, 2-butoxy- (1) - Liquid |
|---|---|
| 298.15 | 0.2692 |
| 311.15 | 0.9038 |
| 332.15 | 4.271 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.2000 | 0.0018 |
| 303.15 | 0.2000 | 0.0016 |
| 308.15 | 0.2000 | 0.0015 |
| 313.15 | 0.2000 | 0.0013 |
| 298.15 | 0.4000 | 0.0030 |
| 303.15 | 0.4000 | 0.0026 |
| 308.15 | 0.4000 | 0.0023 |
| 313.15 | 0.4000 | 0.0021 |
| 298.15 | 0.6000 | 0.0039 |
| 303.15 | 0.6000 | 0.0034 |
| 308.15 | 0.6000 | 0.0029 |
| 313.15 | 0.6000 | 0.0025 |
| 298.15 | 1.0000 | 0.0028 |
| 303.15 | 1.0000 | 0.0025 |
| 308.15 | 1.0000 | 0.0022 |
| 313.15 | 1.0000 | 0.0019 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.0000 | 0.0013 |
| 283.15 | 0.1003 | 0.0055 |
| 283.15 | 0.2000 | 0.0071 |
| 283.15 | 0.3000 | 0.0074 |
| 283.15 | 0.4000 | 0.0072 |
| 283.15 | 0.5000 | 0.0068 |
| 283.15 | 0.6000 | 0.0064 |
| 283.15 | 0.7000 | 0.0059 |
| 283.15 | 0.7999 | 0.0054 |
| 283.15 | 0.9000 | 0.0049 |
| 283.15 | 1.0000 | 0.0045 |
| 293.15 | 0.0000 | 0.0010 |
| 293.15 | 0.1003 | 0.0038 |
| 293.15 | 0.2000 | 0.0049 |
| 293.15 | 0.3000 | 0.0051 |
| 293.15 | 0.4000 | 0.0050 |
| 293.15 | 0.5000 | 0.0048 |
| 293.15 | 0.6000 | 0.0045 |
| 293.15 | 0.7000 | 0.0042 |
| 293.15 | 0.7999 | 0.0039 |
| 293.15 | 0.9000 | 0.0036 |
| 293.15 | 1.0000 | 0.0033 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.1003 | 0.0028 |
| 303.15 | 0.2000 | 0.0035 |
| 303.15 | 0.3000 | 0.0036 |
| 303.15 | 0.4000 | 0.0036 |
| 303.15 | 0.5000 | 0.0034 |
| 303.15 | 0.6000 | 0.0033 |
| 303.15 | 0.7000 | 0.0031 |
| 303.15 | 0.7999 | 0.0029 |
| 303.15 | 0.9000 | 0.0027 |
| 303.15 | 1.0000 | 0.0025 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.1003 | 0.0021 |
| 313.15 | 0.2000 | 0.0026 |
| 313.15 | 0.3000 | 0.0027 |
| 313.15 | 0.4000 | 0.0027 |
| 313.15 | 0.5000 | 0.0026 |
| 313.15 | 0.6000 | 0.0025 |
| 313.15 | 0.7000 | 0.0023 |
| 313.15 | 0.7999 | 0.0022 |
| 313.15 | 0.9000 | 0.0021 |
| 313.15 | 1.0000 | 0.0019 |
| 323.15 | 0.0000 | 0.0005 |
| 323.15 | 0.2000 | 0.0020 |
| 323.15 | 0.3000 | 0.0021 |
| 323.15 | 0.4000 | 0.0020 |
| 323.15 | 0.5000 | 0.0020 |
| 323.15 | 0.6000 | 0.0019 |
| 323.15 | 0.7000 | 0.0018 |
| 323.15 | 0.7999 | 0.0017 |
| 323.15 | 0.9000 | 0.0016 |
| 323.15 | 1.0000 | 0.0015 |
Viscosity, Pa*s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0100 | 0.0011 |
| 0.0250 | 0.0015 |
| 0.0500 | 0.0022 |
| 0.0750 | 0.0028 |
| 0.1000 | 0.0032 |
| 0.1500 | 0.0037 |
| 0.2000 | 0.0040 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0170 | 0.0013 |
| 298.15 | 0.0370 | 0.0018 |
| 298.15 | 0.0610 | 0.0024 |
| 298.15 | 0.0920 | 0.0030 |
| 298.15 | 0.1320 | 0.0039 |
| 298.15 | 1.0000 | 0.0028 |
| 303.15 | 0.0170 | 0.0011 |
| 303.15 | 0.0370 | 0.0016 |
| 303.15 | 0.0610 | 0.0022 |
| 303.15 | 0.0920 | 0.0026 |
| 303.15 | 0.1320 | 0.0034 |
| 303.15 | 1.0000 | 0.0025 |
| 308.15 | 0.0170 | 0.0010 |
| 308.15 | 0.0370 | 0.0015 |
| 308.15 | 0.0610 | 0.0019 |
| 308.15 | 0.0920 | 0.0023 |
| 308.15 | 0.1320 | 0.0029 |
| 308.15 | 1.0000 | 0.0022 |
| 313.15 | 0.0170 | 0.0009 |
| 313.15 | 0.0370 | 0.0013 |
| 313.15 | 0.0610 | 0.0018 |
| 313.15 | 0.0920 | 0.0021 |
| 313.15 | 0.1320 | 0.0025 |
| 313.15 | 1.0000 | 0.0019 |
Relative permittivity at zero frequency [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Relative permittivity at zero frequency - Liquid |
|---|---|
| 0.0100 | 74.74 |
| 0.0250 | 68.67 |
| 0.0500 | 58.85 |
| 0.0750 | 50.77 |
| 0.1000 | 44.78 |
| 0.1500 | 36.81 |
| 0.2000 | 30.4 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 283.15 | 0.0000 | 1.3337 |
| 283.15 | 0.1003 | 1.3785 |
| 283.15 | 0.2000 | 1.3965 |
| 283.15 | 0.3000 | 1.4061 |
| 283.15 | 0.4000 | 1.4118 |
| 283.15 | 0.5000 | 1.4156 |
| 283.15 | 0.6000 | 1.4182 |
| 283.15 | 0.7000 | 1.4199 |
| 283.15 | 0.7999 | 1.4212 |
| 283.15 | 0.9000 | 1.4221 |
| 283.15 | 1.0000 | 1.4226 |
| 293.15 | 0.0000 | 1.333 |
| 293.15 | 0.1003 | 1.3766 |
| 293.15 | 0.2000 | 1.3942 |
| 293.15 | 0.3000 | 1.4036 |
| 293.15 | 0.4000 | 1.4091 |
| 293.15 | 0.5000 | 1.4128 |
| 293.15 | 0.6000 | 1.4153 |
| 293.15 | 0.7000 | 1.4169 |
| 293.15 | 0.7999 | 1.4182 |
| 293.15 | 0.9000 | 1.419 |
| 293.15 | 1.0000 | 1.4196 |
| 303.15 | 0.0000 | 1.3319 |
| 303.15 | 0.1003 | 1.374 |
| 303.15 | 0.2000 | 1.3912 |
| 303.15 | 0.3000 | 1.4002 |
| 303.15 | 0.4000 | 1.4056 |
| 303.15 | 0.5000 | 1.4092 |
| 303.15 | 0.6000 | 1.4116 |
| 303.15 | 0.7000 | 1.4131 |
| 303.15 | 0.7999 | 1.4143 |
| 303.15 | 0.9000 | 1.4152 |
| 303.15 | 1.0000 | 1.4157 |
| 313.15 | 0.0000 | 1.3306 |
| 313.15 | 0.1003 | 1.3712 |
| 313.15 | 0.2000 | 1.3878 |
| 313.15 | 0.3000 | 1.3965 |
| 313.15 | 0.4000 | 1.4018 |
| 313.15 | 0.5000 | 1.4052 |
| 313.15 | 0.6000 | 1.4075 |
| 313.15 | 0.7000 | 1.409 |
| 313.15 | 0.7999 | 1.4101 |
| 313.15 | 0.9000 | 1.4109 |
| 313.15 | 1.0000 | 1.4114 |
| 323.15 | 0.0000 | 1.329 |
| 323.15 | 0.2000 | 1.3839 |
| 323.15 | 0.3000 | 1.3925 |
| 323.15 | 0.4000 | 1.3976 |
| 323.15 | 0.5000 | 1.401 |
| 323.15 | 0.6000 | 1.4032 |
| 323.15 | 0.7000 | 1.4046 |
| 323.15 | 0.7999 | 1.4058 |
| 323.15 | 0.9000 | 1.4066 |
| 323.15 | 1.0000 | 1.407 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0000 | 1.3325 |
| 0.0050 | 1.3361 |
| 0.0075 | 1.3393 |
| 0.0124 | 1.3421 |
| 0.0249 | 1.349 |
| 0.0502 | 1.3601 |
| 0.0748 | 1.3688 |
| 0.1187 | 1.3803 |
| 0.1486 | 1.3867 |
| 0.1993 | 1.3931 |
| 0.2969 | 1.4041 |
| 0.4011 | 1.4075 |
| 0.4975 | 1.4109 |
| 0.5981 | 1.413 |
| 0.7004 | 1.4155 |
| 0.7937 | 1.4167 |
| 0.9107 | 1.4168 |
| 1.0000 | 1.4171 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.0000 | 999.699 |
| 283.15 | 0.0009 | 999.515 |
| 283.15 | 0.0013 | 999.44 |
| 283.15 | 0.0017 | 999.376 |
| 283.15 | 0.0019 | 999.379 |
| 283.15 | 0.0038 | 999.137 |
| 283.15 | 0.0070 | 998.855 |
| 283.15 | 0.0100 | 998.677 |
| 283.15 | 0.0132 | 998.516 |
| 288.15 | 0.0000 | 999.099 |
| 288.15 | 0.0009 | 998.873 |
| 288.15 | 0.0013 | 998.804 |
| 288.15 | 0.0017 | 998.733 |
| 288.15 | 0.0019 | 998.742 |
| 288.15 | 0.0038 | 998.449 |
| 288.15 | 0.0070 | 998.058 |
| 288.15 | 0.0100 | 997.764 |
| 288.15 | 0.0132 | 997.453 |
| 293.15 | 0.0000 | 998.203 |
| 293.15 | 0.0009 | 997.98 |
| 293.15 | 0.0013 | 997.897 |
| 293.15 | 0.0017 | 997.814 |
| 293.15 | 0.0019 | 997.774 |
| 293.15 | 0.0038 | 997.436 |
| 293.15 | 0.0070 | 996.956 |
| 293.15 | 0.0100 | 996.553 |
| 293.15 | 0.0132 | 996.129 |
| 298.15 | 0.0000 | 997.043 |
| 298.15 | 0.0009 | 996.815 |
| 298.15 | 0.0013 | 996.726 |
| 298.15 | 0.0017 | 996.633 |
| 298.15 | 0.0019 | 996.592 |
| 298.15 | 0.0038 | 996.204 |
| 298.15 | 0.0070 | 995.629 |
| 298.15 | 0.0100 | 995.12 |
| 298.15 | 0.0132 | 994.56 |
| 303.15 | 0.0000 | 995.645 |
| 303.15 | 0.0009 | 995.386 |
| 303.15 | 0.0013 | 995.295 |
| 303.15 | 0.0017 | 995.201 |
| 303.15 | 0.0019 | 995.143 |
| 303.15 | 0.0038 | 994.715 |
| 303.15 | 0.0070 | 994.053 |
| 303.15 | 0.0100 | 993.447 |
| 303.15 | 0.0132 | 992.75 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mass fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.2000 | 986.46 |
| 303.15 | 0.2000 | 982.92 |
| 308.15 | 0.2000 | 980.38 |
| 313.15 | 0.2000 | 977.64 |
| 298.15 | 0.4000 | 967.1 |
| 303.15 | 0.4000 | 964.31 |
| 308.15 | 0.4000 | 961.45 |
| 313.15 | 0.4000 | 958.48 |
| 298.15 | 0.6000 | 948.1 |
| 303.15 | 0.6000 | 944.74 |
| 308.15 | 0.6000 | 941.59 |
| 313.15 | 0.6000 | 937.57 |
| 298.15 | 1.0000 | 896.16 |
| 303.15 | 1.0000 | 892.74 |
| 308.15 | 1.0000 | 888.88 |
| 313.15 | 1.0000 | 884.29 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.0000 | 999.7 |
| 283.15 | 0.0005 | 999.62 |
| 283.15 | 0.0010 | 999.53 |
| 283.15 | 0.0020 | 999.43 |
| 283.15 | 0.0030 | 999.37 |
| 283.15 | 0.0040 | 999.24 |
| 283.15 | 0.0050 | 999.06 |
| 283.15 | 0.0060 | 998.89 |
| 283.15 | 0.0070 | 998.86 |
| 283.15 | 0.0080 | 998.8 |
| 283.15 | 0.0090 | 998.72 |
| 283.15 | 0.0100 | 998.68 |
| 283.15 | 0.0110 | 998.64 |
| 283.15 | 0.0121 | 998.59 |
| 283.15 | 0.0132 | 998.55 |
| 283.15 | 0.0140 | 998.49 |
| 283.15 | 0.0150 | 998.49 |
| 283.15 | 0.0196 | 998.45 |
| 283.15 | 0.0253 | 997.0 |
| 283.15 | 0.0307 | 995.31 |
| 283.15 | 0.0350 | 993.94 |
| 283.15 | 0.0405 | 992.16 |
| 283.15 | 0.0452 | 990.59 |
| 283.15 | 0.0496 | 989.23 |
| 283.15 | 0.0599 | 986.08 |
| 283.15 | 0.0698 | 983.28 |
| 283.15 | 0.0798 | 980.63 |
| 283.15 | 0.0898 | 978.05 |
| 283.15 | 0.1003 | 975.52 |
| 283.15 | 0.2000 | 957.51 |
| 283.15 | 0.3000 | 945.28 |
| 283.15 | 0.4000 | 935.77 |
| 283.15 | 0.5000 | 928.69 |
| 283.15 | 0.6000 | 923.16 |
| 283.15 | 0.7000 | 918.7 |
| 283.15 | 0.7999 | 915.01 |
| 283.15 | 0.9000 | 912.08 |
| 283.15 | 1.0000 | 909.49 |
| 283.15 | 0.0000 | 999.7 |
| 293.15 | 0.0000 | 998.2 |
| 293.15 | 0.0005 | 998.13 |
| 293.15 | 0.0010 | 998.01 |
| 293.15 | 0.0020 | 997.89 |
| 293.15 | 0.0030 | 997.78 |
| 293.15 | 0.0040 | 997.6 |
| 293.15 | 0.0050 | 997.34 |
| 293.15 | 0.0060 | 997.11 |
| 293.15 | 0.0070 | 996.97 |
| 293.15 | 0.0080 | 996.83 |
| 293.15 | 0.0090 | 996.7 |
| 293.15 | 0.0100 | 996.57 |
| 293.15 | 0.0110 | 996.43 |
| 293.15 | 0.0121 | 996.3 |
| 293.15 | 0.0132 | 996.16 |
| 293.15 | 0.0140 | 996.02 |
| 293.15 | 0.0150 | 995.91 |
| 293.15 | 0.0196 | 994.9 |
| 293.15 | 0.0253 | 992.94 |
| 293.15 | 0.0307 | 990.88 |
| 293.15 | 0.0350 | 989.28 |
| 293.15 | 0.0405 | 987.22 |
| 293.15 | 0.0452 | 985.5 |
| 293.15 | 0.0496 | 983.99 |
| 293.15 | 0.0599 | 980.54 |
| 293.15 | 0.0698 | 977.49 |
| 293.15 | 0.0798 | 974.61 |
| 293.15 | 0.0898 | 971.87 |
| 293.15 | 0.1003 | 969.12 |
| 293.15 | 0.2000 | 950.15 |
| 293.15 | 0.3000 | 937.5 |
| 293.15 | 0.4000 | 927.76 |
| 293.15 | 0.5000 | 920.54 |
| 293.15 | 0.6000 | 914.96 |
| 293.15 | 0.7000 | 910.49 |
| 293.15 | 0.7999 | 906.78 |
| 293.15 | 0.9000 | 903.8 |
| 293.15 | 1.0000 | 901.18 |
| 293.15 | 0.0000 | 998.2 |
| 303.15 | 0.0000 | 995.65 |
| 303.15 | 0.0005 | 995.57 |
| 303.15 | 0.0010 | 995.46 |
| 303.15 | 0.0020 | 995.29 |
| 303.15 | 0.0030 | 995.12 |
| 303.15 | 0.0040 | 994.89 |
| 303.15 | 0.0050 | 994.59 |
| 303.15 | 0.0060 | 994.27 |
| 303.15 | 0.0070 | 994.06 |
| 303.15 | 0.0080 | 993.86 |
| 303.15 | 0.0090 | 993.69 |
| 303.15 | 0.0100 | 993.5 |
| 303.15 | 0.0110 | 993.3 |
| 303.15 | 0.0121 | 993.09 |
| 303.15 | 0.0132 | 992.85 |
| 303.15 | 0.0140 | 992.63 |
| 303.15 | 0.0150 | 992.38 |
| 303.15 | 0.0196 | 990.79 |
| 303.15 | 0.0253 | 988.38 |
| 303.15 | 0.0307 | 986.03 |
| 303.15 | 0.0350 | 984.22 |
| 303.15 | 0.0405 | 981.99 |
| 303.15 | 0.0452 | 980.12 |
| 303.15 | 0.0496 | 978.47 |
| 303.15 | 0.0599 | 974.75 |
| 303.15 | 0.0698 | 971.48 |
| 303.15 | 0.0798 | 968.38 |
| 303.15 | 0.0898 | 965.46 |
| 303.15 | 0.1003 | 962.59 |
| 303.15 | 0.2000 | 942.62 |
| 303.15 | 0.3000 | 929.57 |
| 303.15 | 0.4000 | 919.6 |
| 303.15 | 0.5000 | 912.16 |
| 303.15 | 0.6000 | 906.6 |
| 303.15 | 0.7000 | 902.02 |
| 303.15 | 0.7999 | 898.3 |
| 303.15 | 0.9000 | 895.3 |
| 303.15 | 1.0000 | 892.68 |
| 303.15 | 0.0000 | 995.65 |
| 313.15 | 0.0000 | 992.21 |
| 313.15 | 0.0005 | 992.12 |
| 313.15 | 0.0010 | 992.02 |
| 313.15 | 0.0020 | 991.8 |
| 313.15 | 0.0030 | 991.58 |
| 313.15 | 0.0040 | 991.31 |
| 313.15 | 0.0050 | 990.98 |
| 313.15 | 0.0060 | 990.64 |
| 313.15 | 0.0070 | 990.36 |
| 313.15 | 0.0080 | 990.11 |
| 313.15 | 0.0090 | 989.86 |
| 313.15 | 0.0100 | 989.6 |
| 313.15 | 0.0110 | 989.31 |
| 313.15 | 0.0121 | 988.99 |
| 313.15 | 0.0132 | 988.65 |
| 313.15 | 0.0140 | 988.37 |
| 313.15 | 0.0150 | 988.01 |
| 313.15 | 0.0196 | 985.95 |
| 313.15 | 0.0253 | 983.21 |
| 313.15 | 0.0307 | 980.66 |
| 313.15 | 0.0350 | 978.71 |
| 313.15 | 0.0405 | 976.24 |
| 313.15 | 0.0452 | 974.25 |
| 313.15 | 0.0496 | 972.5 |
| 313.15 | 0.0599 | 968.52 |
| 313.15 | 0.0698 | 965.02 |
| 313.15 | 0.0798 | 961.77 |
| 313.15 | 0.0898 | 958.67 |
| 313.15 | 0.1003 | 955.66 |
| 313.15 | 0.2000 | 934.8 |
| 313.15 | 0.3000 | 921.47 |
| 313.15 | 0.4000 | 911.3 |
| 313.15 | 0.5000 | 903.78 |
| 313.15 | 0.6000 | 898.14 |
| 313.15 | 0.7000 | 893.57 |
| 313.15 | 0.7999 | 889.84 |
| 313.15 | 0.9000 | 886.83 |
| 313.15 | 1.0000 | 884.21 |
| 313.15 | 0.0000 | 992.21 |
| 323.15 | 0.0000 | 988.04 |
| 323.15 | 0.2000 | 926.83 |
| 323.15 | 0.3000 | 913.23 |
| 323.15 | 0.4000 | 902.87 |
| 323.15 | 0.5000 | 895.22 |
| 323.15 | 0.6000 | 889.56 |
| 323.15 | 0.7000 | 884.96 |
| 323.15 | 0.7999 | 881.26 |
| 323.15 | 0.9000 | 878.23 |
| 323.15 | 1.0000 | 875.6 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 997.05 |
| 0.0050 | 995.62 |
| 0.0075 | 995.08 |
| 0.0124 | 994.34 |
| 0.0249 | 990.15 |
| 0.0502 | 980.52 |
| 0.0748 | 971.93 |
| 0.1187 | 960.53 |
| 0.1486 | 954.18 |
| 0.1993 | 945.3 |
| 0.2969 | 932.71 |
| 0.4011 | 923.1 |
| 0.4975 | 916.23 |
| 0.5981 | 910.49 |
| 0.7004 | 905.8 |
| 0.7937 | 902.23 |
| 0.9107 | 898.33 |
| 1.0000 | 895.79 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0100 | 995.114 |
| 0.0250 | 990.681 |
| 0.0500 | 980.926 |
| 0.0750 | 972.624 |
| 0.1000 | 965.618 |
| 0.1500 | 954.656 |
| 0.2000 | 946.363 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0170 | 993.26 |
| 298.15 | 0.0610 | 976.33 |
| 303.15 | 0.0610 | 974.23 |
| 298.15 | 0.0920 | 967.1 |
| 303.15 | 0.0170 | 990.82 |
| 303.15 | 0.0370 | 982.92 |
| 298.15 | 0.0370 | 986.46 |
| 303.15 | 0.0920 | 964.31 |
| 308.15 | 0.0170 | 988.89 |
| 308.15 | 0.0370 | 980.38 |
| 308.15 | 0.0610 | 971.37 |
| 308.15 | 0.0920 | 961.45 |
| 313.15 | 0.0170 | 985.94 |
| 313.15 | 0.0370 | 977.64 |
| 313.15 | 0.0610 | 968.64 |
| 313.15 | 0.0920 | 958.48 |
| 308.15 | 1.0000 | 888.88 |
| 298.15 | 1.0000 | 896.16 |
| 303.15 | 1.0000 | 892.74 |
| 313.15 | 1.0000 | 884.29 |
| 303.15 | 0.1320 | 944.74 |
| 298.15 | 0.1320 | 948.1 |
| 313.15 | 0.1320 | 937.57 |
| 308.15 | 0.1320 | 941.59 |
Speed of sound, m/s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
|---|---|
| 0.0000 | 1496.7 |
| 0.0050 | 1521.8 |
| 0.0075 | 1536.0 |
| 0.0124 | 1552.6 |
| 0.0249 | 1538.3 |
| 0.0502 | 1506.7 |
| 0.0748 | 1481.8 |
| 0.1187 | 1455.1 |
| 0.1486 | 1442.7 |
| 0.1993 | 1424.9 |
| 0.2969 | 1398.2 |
| 0.4011 | 1376.0 |
| 0.4975 | 1361.8 |
| 0.5981 | 1346.7 |
| 0.7004 | 1335.5 |
| 0.7937 | 1323.4 |
| 0.9107 | 1313.2 |
| 1.0000 | 1308.7 |
Thermal conductivity, W/m/K [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Thermal conductivity, W/m/K - Liquid |
| 304.15 | 100.00 | 0.0478 | 0.4533 |
| 304.15 | 100.00 | 0.1732 | 0.2813 |
| 304.15 | 100.00 | 0.5000 | 0.1837 |
| 304.15 | 100.00 | 0.7500 | 0.1655 |
| 304.15 | 10300.00 | 0.5000 | 0.1877 |
| 304.15 | 10300.00 | 0.7500 | 0.1690 |
| 304.15 | 14200.00 | 0.0478 | 0.4568 |
| 304.15 | 15000.00 | 0.5000 | 0.1890 |
| 304.15 | 19300.00 | 0.7500 | 0.1717 |
| 304.15 | 20300.00 | 0.1732 | 0.2857 |
| 304.15 | 26700.00 | 0.5000 | 0.1936 |
| 304.15 | 27300.00 | 0.0478 | 0.4622 |
| 304.15 | 30000.00 | 0.1732 | 0.2896 |
| 304.15 | 39500.00 | 0.7500 | 0.1771 |
| 304.15 | 41800.00 | 0.0478 | 0.4680 |
| 304.15 | 41800.00 | 0.5000 | 0.1963 |
| 304.15 | 47200.00 | 0.1732 | 0.2942 |
| 304.15 | 54700.00 | 0.5000 | 0.1995 |
| 304.15 | 54700.00 | 0.7500 | 0.1812 |
| 304.15 | 55400.00 | 0.0478 | 0.4704 |
| 304.15 | 70100.00 | 0.0478 | 0.4758 |
| 304.15 | 70200.00 | 0.1732 | 0.3008 |
| 304.15 | 70200.00 | 0.5000 | 0.2032 |
| 304.15 | 76500.00 | 0.7500 | 0.1862 |
| 304.15 | 83900.00 | 0.0478 | 0.4780 |
| 304.15 | 84200.00 | 0.1732 | 0.3043 |
| 304.15 | 84200.00 | 0.5000 | 0.2066 |
| 304.15 | 91200.00 | 0.7500 | 0.1900 |
| 304.15 | 98200.00 | 0.0478 | 0.4845 |
| 304.15 | 98200.00 | 0.1732 | 0.3077 |
| 304.15 | 98200.00 | 0.7500 | 0.1901 |
| 304.15 | 108700.00 | 0.5000 | 0.2127 |
| 304.15 | 110400.00 | 0.1732 | 0.3110 |
| 304.15 | 112100.00 | 0.0478 | 0.4875 |
| 304.15 | 112200.00 | 0.7500 | 0.1951 |
| 304.15 | 124800.00 | 0.5000 | 0.2157 |
| 304.15 | 126000.00 | 0.0478 | 0.4917 |
| 304.15 | 126200.00 | 0.1732 | 0.3147 |
| 304.15 | 127600.00 | 0.7500 | 0.1976 |
| 304.15 | 138700.00 | 0.0478 | 0.4958 |
| 304.15 | 140100.00 | 0.1732 | 0.3175 |
| 304.15 | 140100.00 | 0.5000 | 0.2189 |
| 304.15 | 140100.00 | 0.7500 | 0.2005 |
| 304.15 | 150600.00 | 0.1732 | 0.3195 |
| 304.15 | 150600.00 | 0.7500 | 0.2022 |
| 317.15 | 100.00 | 0.0478 | 0.4606 |
| 317.15 | 16400.00 | 0.0478 | 0.4669 |
| 317.15 | 25500.00 | 0.0478 | 0.4697 |
| 317.15 | 41800.00 | 0.0478 | 0.4750 |
| 317.15 | 56100.00 | 0.0478 | 0.4789 |
| 317.15 | 70600.00 | 0.0478 | 0.4850 |
| 317.15 | 84200.00 | 0.0478 | 0.4875 |
| 317.15 | 98200.00 | 0.0478 | 0.4926 |
| 317.15 | 112200.00 | 0.0478 | 0.4983 |
| 317.15 | 124000.00 | 0.0478 | 0.5008 |
| 317.15 | 141000.00 | 0.0478 | 0.5066 |
| 320.90 | 100.00 | 0.0478 | 0.4774 |
| 320.90 | 2300.00 | 0.0478 | 0.4714 |
| 320.90 | 5000.00 | 0.0478 | 0.4639 |
| 320.90 | 7500.00 | 0.0478 | 0.4677 |
| 320.90 | 10000.00 | 0.0478 | 0.4694 |
| 320.90 | 12500.00 | 0.0478 | 0.4703 |
| 320.90 | 15000.00 | 0.0478 | 0.4705 |
| 320.90 | 19500.00 | 0.0478 | 0.4737 |
| 320.90 | 20000.00 | 0.0478 | 0.4742 |
| 320.90 | 29800.00 | 0.0478 | 0.4774 |
| 320.90 | 52500.00 | 0.0478 | 0.4855 |
| 320.90 | 70200.00 | 0.0478 | 0.4855 |
| 320.90 | 87700.00 | 0.0478 | 0.4986 |
| 320.90 | 105200.00 | 0.0478 | 0.5044 |
| 320.90 | 126200.00 | 0.0478 | 0.5123 |
| 321.15 | 100.00 | 0.5000 | 0.1829 |
| 321.15 | 100.00 | 0.7500 | 0.1624 |
| 321.15 | 10000.00 | 0.5000 | 0.1864 |
| 321.15 | 10000.00 | 0.7500 | 0.1656 |
| 321.15 | 19300.00 | 0.5000 | 0.1892 |
| 321.15 | 19300.00 | 0.7500 | 0.1693 |
| 321.15 | 19700.00 | 0.5000 | 0.1896 |
| 321.15 | 28300.00 | 0.7500 | 0.1718 |
| 321.15 | 39300.00 | 0.7500 | 0.1744 |
| 321.15 | 41800.00 | 0.5000 | 0.1959 |
| 321.15 | 56100.00 | 0.5000 | 0.2001 |
| 321.15 | 56100.00 | 0.7500 | 0.1792 |
| 321.15 | 70200.00 | 0.5000 | 0.2034 |
| 321.15 | 71600.00 | 0.7500 | 0.1836 |
| 321.15 | 84200.00 | 0.5000 | 0.2073 |
| 321.15 | 84200.00 | 0.7500 | 0.1871 |
| 321.15 | 96500.00 | 0.5000 | 0.2099 |
| 321.15 | 98900.00 | 0.7500 | 0.1907 |
| 321.15 | 111500.00 | 0.7500 | 0.1929 |
| 321.15 | 112200.00 | 0.5000 | 0.2144 |
| 321.15 | 124800.00 | 0.7500 | 0.1959 |
| 321.15 | 126900.00 | 0.5000 | 0.2172 |
| 321.15 | 141500.00 | 0.5000 | 0.2201 |
| 321.15 | 142200.00 | 0.7500 | 0.1998 |
| 321.15 | 149900.00 | 0.5000 | 0.2213 |
| 321.15 | 150600.00 | 0.7500 | 0.2016 |
| 322.00 | 100.00 | 0.0478 | 0.4932 |
| 322.00 | 5400.00 | 0.0478 | 0.4886 |
| 322.00 | 20000.00 | 0.0478 | 0.4931 |
| 322.00 | 34600.00 | 0.0478 | 0.5006 |
| 322.00 | 52500.00 | 0.0478 | 0.5069 |
| 322.00 | 70200.00 | 0.0478 | 0.5149 |
| 322.00 | 87700.00 | 0.0478 | 0.5221 |
| 322.00 | 105200.00 | 0.0478 | 0.5280 |
| 322.00 | 119200.00 | 0.0478 | 0.5322 |
| 322.00 | 133200.00 | 0.0478 | 0.5354 |
| 335.00 | 100.00 | 0.1732 | 0.2804 |
| 335.00 | 10000.00 | 0.1732 | 0.2851 |
| 335.00 | 19000.00 | 0.1732 | 0.2895 |
| 335.00 | 41800.00 | 0.1732 | 0.2972 |
| 335.00 | 70200.00 | 0.1732 | 0.3060 |
| 335.00 | 84200.00 | 0.1732 | 0.3077 |
| 335.00 | 98200.00 | 0.1732 | 0.3111 |
| 335.00 | 112200.00 | 0.1732 | 0.3153 |
| 335.00 | 125500.00 | 0.1732 | 0.3205 |
| 335.00 | 137300.00 | 0.1732 | 0.3218 |
| 338.15 | 100.00 | 0.5000 | 0.1796 |
| 338.15 | 100.00 | 0.7500 | 0.1594 |
| 338.15 | 10400.00 | 0.5000 | 0.1841 |
| 338.15 | 11000.00 | 0.7500 | 0.1637 |
| 338.15 | 19000.00 | 0.5000 | 0.1866 |
| 338.15 | 19500.00 | 0.5000 | 0.1867 |
| 338.15 | 19500.00 | 0.7500 | 0.1663 |
| 338.15 | 30700.00 | 0.7500 | 0.1702 |
| 338.15 | 39300.00 | 0.7500 | 0.1723 |
| 338.15 | 41800.00 | 0.5000 | 0.1936 |
| 338.15 | 56100.00 | 0.5000 | 0.1986 |
| 338.15 | 56100.00 | 0.7500 | 0.1767 |
| 338.15 | 70200.00 | 0.5000 | 0.2018 |
| 338.15 | 70200.00 | 0.7500 | 0.1812 |
| 338.15 | 80700.00 | 0.5000 | 0.2039 |
| 338.15 | 91200.00 | 0.7500 | 0.1868 |
| 338.15 | 98200.00 | 0.5000 | 0.2083 |
| 338.15 | 105200.00 | 0.7500 | 0.1907 |
| 338.15 | 112200.00 | 0.5000 | 0.2118 |
| 338.15 | 117800.00 | 0.7500 | 0.1924 |
| 338.15 | 126200.00 | 0.5000 | 0.2146 |
| 338.15 | 131800.00 | 0.7500 | 0.1964 |
| 338.15 | 140800.00 | 0.5000 | 0.2183 |
| 338.15 | 147100.00 | 0.7500 | 0.1997 |
| 346.50 | 100.00 | 0.1732 | 0.2659 |
| 346.50 | 10000.00 | 0.1732 | 0.2753 |
| 346.50 | 20000.00 | 0.1732 | 0.2796 |
| 346.50 | 29500.00 | 0.1732 | 0.2834 |
| 346.50 | 49000.00 | 0.1732 | 0.2904 |
| 346.50 | 84200.00 | 0.1732 | 0.3009 |
| 346.50 | 98200.00 | 0.1732 | 0.3029 |
| 346.50 | 112200.00 | 0.1732 | 0.3046 |
| 346.50 | 122700.00 | 0.1732 | 0.3100 |
| 346.50 | 140100.00 | 0.1732 | 0.3122 |
| 346.50 | 148500.00 | 0.1732 | 0.3128 |
Sources
- Group-contribution to limiting partial molar isentropic compressions of small amphiphile molecules in water. The temperature effect
- Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
- Conductance Studies of NaCl, KCl, NaBr, NaI, NaBPh4, Bu4NI, and NaClO4 in Water + 2-Butoxyethanol Mixtures at T = 298.15 K
- Thermal Conductivity of Aqueous Mixtures of 2-n-Butoxyethanol at Pressures up to 150 MPa
- Conductance Studies of Tetrabutylammonium Bromide, Sodium Bromide, and Sodium Tetraphenylborate in 2-Butoxyethanol (1) + Water (2) Mixtures at (298.15, 303.15, 308.15, and 313.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Electrical Conductance of Some Tetraalkylammonium Bromide Salts in 2-Butoxyethanol (1) + Water (2) mixtures at (298.15, 303.15, 308.15, and 313.15) K
- Density, Viscosity, and Refractive Index for Water + 2-Butoxyethanol and + 2-(2-Butoxyethoxy)ethanol at Various Temperatures
- Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
Note: These property values are available through the Cheméo API. A free account gives you an access key.