- Name
- 1-Octanol
- InChI
- InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3
- InChI Key
- KBPLFHHGFOOTCA-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCCCCCO
- Mol. Weight (g/mol)
- 130.23
- CAS
- 111-87-5
- 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
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Datasets
- η - Viscosity, Pa*s (4)
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (6)
- Tfus - Solid-liquid equilibrium temperature, K (4)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.1199 | 0.0111 |
| 298.15 | 0.3407 | 0.0102 |
| 298.15 | 0.5487 | 0.0093 |
| 298.15 | 0.7394 | 0.0086 |
| 298.15 | 0.9180 | 0.0079 |
| 308.15 | 0.1199 | 0.0078 |
| 308.15 | 0.3407 | 0.0072 |
| 308.15 | 0.5487 | 0.0066 |
| 308.15 | 0.7394 | 0.0061 |
| 308.15 | 0.9180 | 0.0057 |
| 318.15 | 0.1199 | 0.0056 |
| 318.15 | 0.3407 | 0.0052 |
| 318.15 | 0.5487 | 0.0048 |
| 318.15 | 0.7394 | 0.0044 |
| 318.15 | 0.9180 | 0.0041 |
| 328.15 | 0.1199 | 0.0041 |
| 328.15 | 0.3407 | 0.0038 |
| 328.15 | 0.5487 | 0.0036 |
| 328.15 | 0.7394 | 0.0033 |
| 328.15 | 0.9180 | 0.0031 |
| 338.15 | 0.1199 | 0.0031 |
| 338.15 | 0.3407 | 0.0029 |
| 338.15 | 0.5487 | 0.0027 |
| 338.15 | 0.7394 | 0.0025 |
| 338.15 | 0.9180 | 0.0024 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.0000 | 0.0221 |
| 283.15 | 0.0995 | 0.0211 |
| 283.15 | 0.1998 | 0.0202 |
| 283.15 | 0.3007 | 0.0194 |
| 283.15 | 0.4001 | 0.0185 |
| 283.15 | 0.4996 | 0.0176 |
| 283.15 | 0.5988 | 0.0167 |
| 283.15 | 0.6998 | 0.0158 |
| 283.15 | 0.8001 | 0.0151 |
| 283.15 | 0.9000 | 0.0142 |
| 283.15 | 1.0000 | 0.0135 |
| 288.15 | 0.0000 | 0.0180 |
| 288.15 | 0.0995 | 0.0172 |
| 288.15 | 0.1998 | 0.0165 |
| 288.15 | 0.3007 | 0.0156 |
| 288.15 | 0.4001 | 0.0151 |
| 288.15 | 0.4996 | 0.0142 |
| 288.15 | 0.5988 | 0.0137 |
| 288.15 | 0.6998 | 0.0130 |
| 288.15 | 0.8001 | 0.0122 |
| 288.15 | 0.9000 | 0.0118 |
| 288.15 | 1.0000 | 0.0109 |
| 293.15 | 0.0000 | 0.0144 |
| 293.15 | 0.0995 | 0.0138 |
| 293.15 | 0.1998 | 0.0133 |
| 293.15 | 0.3007 | 0.0127 |
| 293.15 | 0.4001 | 0.0123 |
| 293.15 | 0.4996 | 0.0116 |
| 293.15 | 0.5988 | 0.0111 |
| 293.15 | 0.6998 | 0.0103 |
| 293.15 | 0.8001 | 0.0097 |
| 293.15 | 0.9000 | 0.0090 |
| 293.15 | 1.0000 | 0.0089 |
| 298.15 | 0.0000 | 0.0117 |
| 298.15 | 0.0995 | 0.0113 |
| 298.15 | 0.1998 | 0.0109 |
| 298.15 | 0.3007 | 0.0105 |
| 298.15 | 0.4001 | 0.0101 |
| 298.15 | 0.4996 | 0.0096 |
| 298.15 | 0.5988 | 0.0092 |
| 298.15 | 0.6998 | 0.0088 |
| 298.15 | 0.8001 | 0.0083 |
| 298.15 | 0.9000 | 0.0078 |
| 298.15 | 1.0000 | 0.0075 |
| 303.15 | 0.0000 | 0.0096 |
| 303.15 | 0.0995 | 0.0092 |
| 303.15 | 0.1998 | 0.0089 |
| 303.15 | 0.3007 | 0.0086 |
| 303.15 | 0.4001 | 0.0082 |
| 303.15 | 0.4996 | 0.0079 |
| 303.15 | 0.5988 | 0.0076 |
| 303.15 | 0.6998 | 0.0073 |
| 303.15 | 0.8001 | 0.0070 |
| 303.15 | 0.9000 | 0.0067 |
| 303.15 | 1.0000 | 0.0063 |
| 308.15 | 0.0000 | 0.0080 |
| 308.15 | 0.0995 | 0.0078 |
| 308.15 | 0.1998 | 0.0075 |
| 308.15 | 0.3007 | 0.0072 |
| 308.15 | 0.4001 | 0.0070 |
| 308.15 | 0.4996 | 0.0067 |
| 308.15 | 0.5988 | 0.0064 |
| 308.15 | 0.6998 | 0.0061 |
| 308.15 | 0.8001 | 0.0059 |
| 308.15 | 0.9000 | 0.0057 |
| 308.15 | 1.0000 | 0.0053 |
| 313.15 | 0.0000 | 0.0068 |
| 313.15 | 0.0995 | 0.0066 |
| 313.15 | 0.1998 | 0.0064 |
| 313.15 | 0.3007 | 0.0062 |
| 313.15 | 0.4001 | 0.0060 |
| 313.15 | 0.4996 | 0.0057 |
| 313.15 | 0.5988 | 0.0055 |
| 313.15 | 0.6998 | 0.0053 |
| 313.15 | 0.8001 | 0.0051 |
| 313.15 | 0.9000 | 0.0048 |
| 313.15 | 1.0000 | 0.0045 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.1199 | 0.0111 |
| 298.15 | 0.3407 | 0.0102 |
| 298.15 | 0.5487 | 0.0093 |
| 298.15 | 0.7394 | 0.0086 |
| 298.15 | 0.9180 | 0.0079 |
| 308.15 | 0.1199 | 0.0078 |
| 308.15 | 0.3407 | 0.0072 |
| 308.15 | 0.5487 | 0.0066 |
| 308.15 | 0.7394 | 0.0061 |
| 308.15 | 0.9180 | 0.0057 |
| 318.15 | 0.1199 | 0.0056 |
| 318.15 | 0.3407 | 0.0052 |
| 318.15 | 0.5487 | 0.0048 |
| 318.15 | 0.7394 | 0.0044 |
| 318.15 | 0.9180 | 0.0041 |
| 328.15 | 0.1199 | 0.0041 |
| 328.15 | 0.3407 | 0.0038 |
| 328.15 | 0.5487 | 0.0036 |
| 328.15 | 0.7394 | 0.0033 |
| 328.15 | 0.9180 | 0.0031 |
| 338.15 | 0.1199 | 0.0031 |
| 338.15 | 0.3407 | 0.0029 |
| 338.15 | 0.5487 | 0.0027 |
| 338.15 | 0.7394 | 0.0025 |
| 338.15 | 0.9180 | 0.0024 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.0000 | 0.0221 |
| 283.15 | 0.0995 | 0.0211 |
| 283.15 | 0.1998 | 0.0202 |
| 283.15 | 0.3007 | 0.0194 |
| 283.15 | 0.4001 | 0.0185 |
| 283.15 | 0.4996 | 0.0176 |
| 283.15 | 0.5988 | 0.0167 |
| 283.15 | 0.6998 | 0.0158 |
| 283.15 | 0.8001 | 0.0151 |
| 283.15 | 0.9000 | 0.0142 |
| 283.15 | 1.0000 | 0.0135 |
| 288.15 | 0.0000 | 0.0180 |
| 288.15 | 0.0995 | 0.0172 |
| 288.15 | 0.1998 | 0.0165 |
| 288.15 | 0.3007 | 0.0156 |
| 288.15 | 0.4001 | 0.0151 |
| 288.15 | 0.4996 | 0.0142 |
| 288.15 | 0.5988 | 0.0137 |
| 288.15 | 0.6998 | 0.0130 |
| 288.15 | 0.8001 | 0.0122 |
| 288.15 | 0.9000 | 0.0118 |
| 288.15 | 1.0000 | 0.0109 |
| 293.15 | 0.0000 | 0.0144 |
| 293.15 | 0.0995 | 0.0138 |
| 293.15 | 0.1998 | 0.0133 |
| 293.15 | 0.3007 | 0.0127 |
| 293.15 | 0.4001 | 0.0123 |
| 293.15 | 0.4996 | 0.0116 |
| 293.15 | 0.5988 | 0.0111 |
| 293.15 | 0.6998 | 0.0103 |
| 293.15 | 0.8001 | 0.0097 |
| 293.15 | 0.9000 | 0.0090 |
| 293.15 | 1.0000 | 0.0089 |
| 298.15 | 0.0000 | 0.0117 |
| 298.15 | 0.0995 | 0.0113 |
| 298.15 | 0.1998 | 0.0109 |
| 298.15 | 0.3007 | 0.0105 |
| 298.15 | 0.4001 | 0.0101 |
| 298.15 | 0.4996 | 0.0096 |
| 298.15 | 0.5988 | 0.0092 |
| 298.15 | 0.6998 | 0.0088 |
| 298.15 | 0.8001 | 0.0083 |
| 298.15 | 0.9000 | 0.0078 |
| 298.15 | 1.0000 | 0.0075 |
| 303.15 | 0.0000 | 0.0096 |
| 303.15 | 0.0995 | 0.0092 |
| 303.15 | 0.1998 | 0.0089 |
| 303.15 | 0.3007 | 0.0086 |
| 303.15 | 0.4001 | 0.0082 |
| 303.15 | 0.4996 | 0.0079 |
| 303.15 | 0.5988 | 0.0076 |
| 303.15 | 0.6998 | 0.0073 |
| 303.15 | 0.8001 | 0.0070 |
| 303.15 | 0.9000 | 0.0067 |
| 303.15 | 1.0000 | 0.0063 |
| 308.15 | 0.0000 | 0.0080 |
| 308.15 | 0.0995 | 0.0078 |
| 308.15 | 0.1998 | 0.0075 |
| 308.15 | 0.3007 | 0.0072 |
| 308.15 | 0.4001 | 0.0070 |
| 308.15 | 0.4996 | 0.0067 |
| 308.15 | 0.5988 | 0.0064 |
| 308.15 | 0.6998 | 0.0061 |
| 308.15 | 0.8001 | 0.0059 |
| 308.15 | 0.9000 | 0.0057 |
| 308.15 | 1.0000 | 0.0053 |
| 313.15 | 0.0000 | 0.0068 |
| 313.15 | 0.0995 | 0.0066 |
| 313.15 | 0.1998 | 0.0064 |
| 313.15 | 0.3007 | 0.0062 |
| 313.15 | 0.4001 | 0.0060 |
| 313.15 | 0.4996 | 0.0057 |
| 313.15 | 0.5988 | 0.0055 |
| 313.15 | 0.6998 | 0.0053 |
| 313.15 | 0.8001 | 0.0051 |
| 313.15 | 0.9000 | 0.0048 |
| 313.15 | 1.0000 | 0.0045 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1-Octanol (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0500 | 1.435 |
| 0.0996 | 1.4346 |
| 0.1996 | 1.434 |
| 0.2997 | 1.4333 |
| 0.4005 | 1.4325 |
| 0.5006 | 1.4318 |
| 0.6005 | 1.431 |
| 0.7006 | 1.4301 |
| 0.8002 | 1.4293 |
| 0.9000 | 1.4284 |
| 0.9507 | 1.4279 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1-Octanol (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0500 | 1.435 |
| 0.0996 | 1.4346 |
| 0.1996 | 1.434 |
| 0.2997 | 1.4333 |
| 0.4005 | 1.4325 |
| 0.5006 | 1.4318 |
| 0.6005 | 1.431 |
| 0.7006 | 1.4301 |
| 0.8002 | 1.4293 |
| 0.9000 | 1.4284 |
| 0.9507 | 1.4279 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.1199 | 826.6 |
| 298.15 | 0.3407 | 825.5 |
| 298.15 | 0.5487 | 824.5 |
| 298.15 | 0.7394 | 823.5 |
| 298.15 | 0.9180 | 822.6 |
| 308.15 | 0.1199 | 819.6 |
| 308.15 | 0.3407 | 818.6 |
| 308.15 | 0.5487 | 817.5 |
| 308.15 | 0.7394 | 816.5 |
| 308.15 | 0.9180 | 815.5 |
| 318.15 | 0.1199 | 812.6 |
| 318.15 | 0.3407 | 811.6 |
| 318.15 | 0.5487 | 810.5 |
| 318.15 | 0.7394 | 809.5 |
| 318.15 | 0.9180 | 808.5 |
| 328.15 | 0.1199 | 805.6 |
| 328.15 | 0.3407 | 804.6 |
| 328.15 | 0.5487 | 803.4 |
| 328.15 | 0.7394 | 802.4 |
| 328.15 | 0.9180 | 801.3 |
| 338.15 | 0.1199 | 798.5 |
| 338.15 | 0.3407 | 797.4 |
| 338.15 | 0.5487 | 796.2 |
| 338.15 | 0.7394 | 795.1 |
| 338.15 | 0.9180 | 794.0 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.0000 | 836.6 |
| 283.15 | 0.0995 | 836.1 |
| 283.15 | 0.1998 | 835.7 |
| 283.15 | 0.3007 | 835.3 |
| 283.15 | 0.4001 | 834.9 |
| 283.15 | 0.4996 | 834.5 |
| 283.15 | 0.5988 | 834.0 |
| 283.15 | 0.6998 | 833.6 |
| 283.15 | 0.8001 | 833.1 |
| 283.15 | 0.9000 | 832.8 |
| 283.15 | 1.0000 | 832.1 |
| 288.15 | 0.0000 | 833.3 |
| 288.15 | 0.0995 | 832.7 |
| 288.15 | 0.1998 | 832.3 |
| 288.15 | 0.3007 | 831.9 |
| 288.15 | 0.4001 | 831.5 |
| 288.15 | 0.4996 | 831.1 |
| 288.15 | 0.5988 | 830.6 |
| 288.15 | 0.6998 | 830.2 |
| 288.15 | 0.8001 | 829.7 |
| 288.15 | 0.9000 | 829.4 |
| 288.15 | 1.0000 | 828.6 |
| 293.15 | 0.0000 | 829.9 |
| 293.15 | 0.0995 | 829.3 |
| 293.15 | 0.1998 | 828.9 |
| 293.15 | 0.3007 | 828.5 |
| 293.15 | 0.4001 | 828.1 |
| 293.15 | 0.4996 | 827.7 |
| 293.15 | 0.5988 | 827.2 |
| 293.15 | 0.6998 | 826.9 |
| 293.15 | 0.8001 | 826.3 |
| 293.15 | 0.9000 | 825.9 |
| 293.15 | 1.0000 | 825.2 |
| 298.15 | 0.0000 | 826.5 |
| 298.15 | 0.0995 | 825.9 |
| 298.15 | 0.1998 | 825.5 |
| 298.15 | 0.3007 | 825.1 |
| 298.15 | 0.4001 | 824.7 |
| 298.15 | 0.4996 | 824.3 |
| 298.15 | 0.5988 | 823.8 |
| 298.15 | 0.6998 | 823.4 |
| 298.15 | 0.8001 | 822.8 |
| 298.15 | 0.9000 | 822.3 |
| 298.15 | 1.0000 | 821.9 |
| 303.15 | 0.0000 | 823.0 |
| 303.15 | 0.0995 | 822.5 |
| 303.15 | 0.1998 | 822.1 |
| 303.15 | 0.3007 | 821.7 |
| 303.15 | 0.4001 | 821.3 |
| 303.15 | 0.4996 | 820.8 |
| 303.15 | 0.5988 | 820.4 |
| 303.15 | 0.6998 | 820.0 |
| 303.15 | 0.8001 | 819.4 |
| 303.15 | 0.9000 | 818.9 |
| 303.15 | 1.0000 | 818.4 |
| 308.15 | 0.0000 | 819.6 |
| 308.15 | 0.0995 | 819.1 |
| 308.15 | 0.1998 | 818.7 |
| 308.15 | 0.3007 | 818.3 |
| 308.15 | 0.4001 | 817.8 |
| 308.15 | 0.4996 | 817.4 |
| 308.15 | 0.5988 | 816.9 |
| 308.15 | 0.6998 | 816.5 |
| 308.15 | 0.8001 | 815.9 |
| 308.15 | 0.9000 | 815.5 |
| 308.15 | 1.0000 | 815.0 |
| 313.15 | 0.0000 | 816.3 |
| 313.15 | 0.0995 | 815.6 |
| 313.15 | 0.1998 | 815.2 |
| 313.15 | 0.3007 | 814.8 |
| 313.15 | 0.4001 | 814.4 |
| 313.15 | 0.4996 | 813.9 |
| 313.15 | 0.5988 | 813.5 |
| 313.15 | 0.6998 | 813.0 |
| 313.15 | 0.8001 | 812.4 |
| 313.15 | 0.9000 | 812.0 |
| 313.15 | 1.0000 | 811.4 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1-Decanol (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0500 | 826.4 |
| 0.0996 | 826.2 |
| 0.1996 | 825.8 |
| 0.2997 | 825.4 |
| 0.4005 | 825.0 |
| 0.5006 | 824.5 |
| 0.6005 | 824.1 |
| 0.7006 | 823.6 |
| 0.8002 | 823.1 |
| 0.9000 | 822.7 |
| 0.9507 | 822.4 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.1199 | 826.6 |
| 298.15 | 0.3407 | 825.5 |
| 298.15 | 0.5487 | 824.5 |
| 298.15 | 0.7394 | 823.5 |
| 298.15 | 0.9180 | 822.6 |
| 308.15 | 0.1199 | 819.6 |
| 308.15 | 0.3407 | 818.6 |
| 308.15 | 0.5487 | 817.5 |
| 308.15 | 0.7394 | 816.5 |
| 308.15 | 0.9180 | 815.5 |
| 318.15 | 0.1199 | 812.6 |
| 318.15 | 0.3407 | 811.6 |
| 318.15 | 0.5487 | 810.5 |
| 318.15 | 0.7394 | 809.5 |
| 318.15 | 0.9180 | 808.5 |
| 328.15 | 0.1199 | 805.6 |
| 328.15 | 0.3407 | 804.6 |
| 328.15 | 0.5487 | 803.4 |
| 328.15 | 0.7394 | 802.4 |
| 328.15 | 0.9180 | 801.3 |
| 338.15 | 0.1199 | 798.5 |
| 338.15 | 0.3407 | 797.4 |
| 338.15 | 0.5487 | 796.2 |
| 338.15 | 0.7394 | 795.1 |
| 338.15 | 0.9180 | 794.0 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Octanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.0000 | 836.6 |
| 283.15 | 0.0995 | 836.1 |
| 283.15 | 0.1998 | 835.7 |
| 283.15 | 0.3007 | 835.3 |
| 283.15 | 0.4001 | 834.9 |
| 283.15 | 0.4996 | 834.5 |
| 283.15 | 0.5988 | 834.0 |
| 283.15 | 0.6998 | 833.6 |
| 283.15 | 0.8001 | 833.1 |
| 283.15 | 0.9000 | 832.8 |
| 283.15 | 1.0000 | 832.1 |
| 288.15 | 0.0000 | 833.3 |
| 288.15 | 0.0995 | 832.7 |
| 288.15 | 0.1998 | 832.3 |
| 288.15 | 0.3007 | 831.9 |
| 288.15 | 0.4001 | 831.5 |
| 288.15 | 0.4996 | 831.1 |
| 288.15 | 0.5988 | 830.6 |
| 288.15 | 0.6998 | 830.2 |
| 288.15 | 0.8001 | 829.7 |
| 288.15 | 0.9000 | 829.4 |
| 288.15 | 1.0000 | 828.6 |
| 293.15 | 0.0000 | 829.9 |
| 293.15 | 0.0995 | 829.3 |
| 293.15 | 0.1998 | 828.9 |
| 293.15 | 0.3007 | 828.5 |
| 293.15 | 0.4001 | 828.1 |
| 293.15 | 0.4996 | 827.7 |
| 293.15 | 0.5988 | 827.2 |
| 293.15 | 0.6998 | 826.9 |
| 293.15 | 0.8001 | 826.3 |
| 293.15 | 0.9000 | 825.9 |
| 293.15 | 1.0000 | 825.2 |
| 298.15 | 0.0000 | 826.5 |
| 298.15 | 0.0995 | 825.9 |
| 298.15 | 0.1998 | 825.5 |
| 298.15 | 0.3007 | 825.1 |
| 298.15 | 0.4001 | 824.7 |
| 298.15 | 0.4996 | 824.3 |
| 298.15 | 0.5988 | 823.8 |
| 298.15 | 0.6998 | 823.4 |
| 298.15 | 0.8001 | 822.8 |
| 298.15 | 0.9000 | 822.3 |
| 298.15 | 1.0000 | 821.9 |
| 303.15 | 0.0000 | 823.0 |
| 303.15 | 0.0995 | 822.5 |
| 303.15 | 0.1998 | 822.1 |
| 303.15 | 0.3007 | 821.7 |
| 303.15 | 0.4001 | 821.3 |
| 303.15 | 0.4996 | 820.8 |
| 303.15 | 0.5988 | 820.4 |
| 303.15 | 0.6998 | 820.0 |
| 303.15 | 0.8001 | 819.4 |
| 303.15 | 0.9000 | 818.9 |
| 303.15 | 1.0000 | 818.4 |
| 308.15 | 0.0000 | 819.6 |
| 308.15 | 0.0995 | 819.1 |
| 308.15 | 0.1998 | 818.7 |
| 308.15 | 0.3007 | 818.3 |
| 308.15 | 0.4001 | 817.8 |
| 308.15 | 0.4996 | 817.4 |
| 308.15 | 0.5988 | 816.9 |
| 308.15 | 0.6998 | 816.5 |
| 308.15 | 0.8001 | 815.9 |
| 308.15 | 0.9000 | 815.5 |
| 308.15 | 1.0000 | 815.0 |
| 313.15 | 0.0000 | 816.3 |
| 313.15 | 0.0995 | 815.6 |
| 313.15 | 0.1998 | 815.2 |
| 313.15 | 0.3007 | 814.8 |
| 313.15 | 0.4001 | 814.4 |
| 313.15 | 0.4996 | 813.9 |
| 313.15 | 0.5988 | 813.5 |
| 313.15 | 0.6998 | 813.0 |
| 313.15 | 0.8001 | 812.4 |
| 313.15 | 0.9000 | 812.0 |
| 313.15 | 1.0000 | 811.4 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of 1-Decanol (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0500 | 826.4 |
| 0.0996 | 826.2 |
| 0.1996 | 825.8 |
| 0.2997 | 825.4 |
| 0.4005 | 825.0 |
| 0.5006 | 824.5 |
| 0.6005 | 824.1 |
| 0.7006 | 823.6 |
| 0.8002 | 823.1 |
| 0.9000 | 822.7 |
| 0.9507 | 822.4 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Octanol (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 280.19 |
| 0.0503 | 278.93 |
| 0.1000 | 278.28 |
| 0.1999 | 275.79 |
| 0.2999 | 272.39 |
| 0.4005 | 269.24 |
| 0.5001 | 265.24 |
| 0.5999 | 260.79 |
| 0.7008 | 255.15 |
| 0.7599 | 251.03 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Octanol (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.7599 | 251.03 |
| 0.7801 | 251.73 |
| 0.7999 | 252.08 |
| 0.9000 | 255.19 |
| 0.9500 | 256.42 |
| 1.0000 | 257.70 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Octanol (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 280.19 |
| 0.0503 | 278.93 |
| 0.1000 | 278.28 |
| 0.1999 | 275.79 |
| 0.2999 | 272.39 |
| 0.4005 | 269.24 |
| 0.5001 | 265.24 |
| 0.5999 | 260.79 |
| 0.7008 | 255.15 |
| 0.7599 | 251.03 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Octanol (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.7599 | 251.03 |
| 0.7801 | 251.73 |
| 0.7999 | 252.08 |
| 0.9000 | 255.19 |
| 0.9500 | 256.42 |
| 1.0000 | 257.70 |
Sources
- SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
- Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
- Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
- Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum