- Name
- Benzyl alcohol
- InChI
- InChI=1S/C7H8O/c8-6-7-4-2-1-3-5-7/h1-5,8H,6H2
- InChI Key
- WVDDGKGOMKODPV-UHFFFAOYSA-N
- Formula
- C7H8O
- SMILES
- OCc1ccccc1
- Mol. Weight (g/mol)
- 108.14
- CAS
- 100-51-6
- Name
- 1-Butanol
- InChI
- InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
- InChI Key
- LRHPLDYGYMQRHN-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CCCCO
- Mol. Weight (g/mol)
- 74.12
- CAS
- 71-36-3
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Datasets
- η - Viscosity, Pa*s (2)
- Excess molar enthalpy (molar enthalpy (2)
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (2)
- γ - Surface tension liquid-gas, N/m (2)
Viscosity, Pa*s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0026 |
| 0.0799 | 0.0027 |
| 0.1607 | 0.0028 |
| 0.2390 | 0.0029 |
| 0.3199 | 0.0031 |
| 0.3995 | 0.0032 |
| 0.4799 | 0.0034 |
| 0.5597 | 0.0037 |
| 0.6396 | 0.0039 |
| 0.7205 | 0.0042 |
| 0.8005 | 0.0045 |
| 0.8800 | 0.0049 |
| 0.9594 | 0.0052 |
| 1.0000 | 0.0054 |
Mole fraction of Benzyl alcohol (1)
Viscosity, Pa*s
2.50e-3
3.00e-3
3.50e-3
4.00e-3
4.50e-3
5.00e-3
5.50e-3
0
0.5
1
Viscosity, Pa*s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0026 |
| 0.0799 | 0.0027 |
| 0.1607 | 0.0028 |
| 0.2390 | 0.0029 |
| 0.3199 | 0.0031 |
| 0.3995 | 0.0032 |
| 0.4799 | 0.0034 |
| 0.5597 | 0.0037 |
| 0.6396 | 0.0039 |
| 0.7205 | 0.0042 |
| 0.8005 | 0.0045 |
| 0.8800 | 0.0049 |
| 0.9594 | 0.0052 |
| 1.0000 | 0.0054 |
Mole fraction of Benzyl alcohol (1)
Viscosity, Pa*s
2.50e-3
3.00e-3
3.50e-3
4.00e-3
4.50e-3
5.00e-3
5.50e-3
0
0.5
1
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0976 | 0.0849 |
| 0.1973 | 0.1489 |
| 0.2950 | 0.1961 |
| 0.3960 | 0.2211 |
| 0.4931 | 0.2311 |
| 0.6029 | 0.2121 |
| 0.7039 | 0.1790 |
| 0.8026 | 0.1328 |
| 0.9017 | 0.0726 |
Mole fraction of Benzyl alcohol (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.1
0.15
0.2
0.2
0.4
0.6000000000000001
0.8
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0976 | 0.0849 |
| 0.1973 | 0.1489 |
| 0.2950 | 0.1961 |
| 0.3960 | 0.2211 |
| 0.4931 | 0.2311 |
| 0.6029 | 0.2121 |
| 0.7039 | 0.1790 |
| 0.8026 | 0.1328 |
| 0.9017 | 0.0726 |
Mole fraction of Benzyl alcohol (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.1
0.15
0.2
0.2
0.4
0.6000000000000001
0.8
Refractive index (Na D-line) [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0000 | 1.3969 |
| 0.0799 | 1.4097 |
| 0.1607 | 1.4224 |
| 0.2390 | 1.4346 |
| 0.3199 | 1.4469 |
| 0.3995 | 1.4588 |
| 0.4799 | 1.4705 |
| 0.5597 | 1.4816 |
| 0.6396 | 1.4924 |
| 0.7205 | 1.5032 |
| 0.8005 | 1.5137 |
| 0.8800 | 1.5238 |
| 0.9594 | 1.5333 |
| 1.0000 | 1.5381 |
Mole fraction of Benzyl alcohol (1)
Refractive index (Na D-line)
1.4
1.42
1.44
1.46
1.48
1.5
1.52
1.54
0
0.5
1
Refractive index (Na D-line) [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0000 | 1.3969 |
| 0.0799 | 1.4097 |
| 0.1607 | 1.4224 |
| 0.2390 | 1.4346 |
| 0.3199 | 1.4469 |
| 0.3995 | 1.4588 |
| 0.4799 | 1.4705 |
| 0.5597 | 1.4816 |
| 0.6396 | 1.4924 |
| 0.7205 | 1.5032 |
| 0.8005 | 1.5137 |
| 0.8800 | 1.5238 |
| 0.9594 | 1.5333 |
| 1.0000 | 1.5381 |
Mole fraction of Benzyl alcohol (1)
Refractive index (Na D-line)
1.4
1.42
1.44
1.46
1.48
1.5
1.52
1.54
0
0.5
1
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 806.07 |
| 0.0824 | 828.7 |
| 0.1602 | 849.52 |
| 0.2392 | 870.06 |
| 0.3206 | 890.78 |
| 0.3990 | 910.07 |
| 0.4803 | 929.52 |
| 0.5586 | 947.83 |
| 0.6394 | 966.22 |
| 0.7198 | 983.97 |
| 0.7993 | 1001.09 |
| 0.8813 | 1018.24 |
| 0.9604 | 1034.25 |
| 1.0000 | 1042.1 |
Mole fraction of Benzyl alcohol (1)
Mass density, kg/m3
800
850
900
950
1000
1050
0
0.5
1
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
| Mole fraction of Benzyl alcohol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 806.07 |
| 0.0824 | 828.7 |
| 0.1602 | 849.52 |
| 0.2392 | 870.06 |
| 0.3206 | 890.78 |
| 0.3990 | 910.07 |
| 0.4803 | 929.52 |
| 0.5586 | 947.83 |
| 0.6394 | 966.22 |
| 0.7198 | 983.97 |
| 0.7993 | 1001.09 |
| 0.8813 | 1018.24 |
| 0.9604 | 1034.25 |
| 1.0000 | 1042.1 |
Mole fraction of Benzyl alcohol (1)
Mass density, kg/m3
800
850
900
950
1000
1050
0
0.5
1
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol (2) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 293.15 | 0.0000 | 0.0391 |
| 293.15 | 0.0034 | 0.0379 |
| 293.15 | 0.0044 | 0.0377 |
| 293.15 | 0.0071 | 0.0371 |
| 293.15 | 0.0117 | 0.0369 |
| 293.15 | 0.0213 | 0.0366 |
| 293.15 | 0.0303 | 0.0365 |
| 293.15 | 0.0492 | 0.0359 |
| 293.15 | 1.0000 | 0.0242 |
| 298.15 | 0.0000 | 0.0386 |
| 298.15 | 0.0034 | 0.0374 |
| 298.15 | 0.0044 | 0.0372 |
| 298.15 | 0.0071 | 0.0367 |
| 298.15 | 0.0117 | 0.0365 |
| 298.15 | 0.0213 | 0.0362 |
| 298.15 | 0.0303 | 0.0360 |
| 298.15 | 0.0492 | 0.0355 |
| 298.15 | 1.0000 | 0.0237 |
| 303.15 | 0.0000 | 0.0381 |
| 303.15 | 0.0034 | 0.0369 |
| 303.15 | 0.0044 | 0.0368 |
| 303.15 | 0.0071 | 0.0362 |
| 303.15 | 0.0117 | 0.0360 |
| 303.15 | 0.0213 | 0.0357 |
| 303.15 | 0.0303 | 0.0355 |
| 303.15 | 0.0492 | 0.0351 |
| 303.15 | 1.0000 | 0.0233 |
| 308.15 | 0.0000 | 0.0376 |
| 308.15 | 0.0034 | 0.0365 |
| 308.15 | 0.0044 | 0.0364 |
| 308.15 | 0.0071 | 0.0358 |
| 308.15 | 0.0117 | 0.0356 |
| 308.15 | 0.0213 | 0.0352 |
| 308.15 | 0.0303 | 0.0350 |
| 308.15 | 0.0492 | 0.0346 |
| 308.15 | 1.0000 | 0.0228 |
| 313.15 | 0.0000 | 0.0372 |
| 313.15 | 0.0034 | 0.0361 |
| 313.15 | 0.0044 | 0.0359 |
| 313.15 | 0.0071 | 0.0353 |
| 313.15 | 0.0117 | 0.0351 |
| 313.15 | 0.0213 | 0.0347 |
| 313.15 | 0.0303 | 0.0346 |
| 313.15 | 0.0492 | 0.0342 |
| 313.15 | 1.0000 | 0.0224 |
| 318.15 | 0.0000 | 0.0366 |
| 318.15 | 0.0034 | 0.0356 |
| 318.15 | 0.0044 | 0.0355 |
| 318.15 | 0.0071 | 0.0348 |
| 318.15 | 0.0117 | 0.0347 |
| 318.15 | 0.0213 | 0.0343 |
| 318.15 | 0.0303 | 0.0340 |
| 318.15 | 0.0492 | 0.0337 |
| 318.15 | 1.0000 | 0.0220 |
| 323.15 | 0.0000 | 0.0362 |
| 323.15 | 0.0034 | 0.0352 |
| 323.15 | 0.0044 | 0.0351 |
| 323.15 | 0.0071 | 0.0344 |
| 323.15 | 0.0117 | 0.0342 |
| 323.15 | 0.0213 | 0.0338 |
| 323.15 | 0.0303 | 0.0336 |
| 323.15 | 0.0492 | 0.0333 |
| 323.15 | 1.0000 | 0.0215 |
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Butanol (2) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 293.15 | 0.0000 | 0.0391 |
| 293.15 | 0.0034 | 0.0379 |
| 293.15 | 0.0044 | 0.0377 |
| 293.15 | 0.0071 | 0.0371 |
| 293.15 | 0.0117 | 0.0369 |
| 293.15 | 0.0213 | 0.0366 |
| 293.15 | 0.0303 | 0.0365 |
| 293.15 | 0.0492 | 0.0359 |
| 293.15 | 1.0000 | 0.0242 |
| 298.15 | 0.0000 | 0.0386 |
| 298.15 | 0.0034 | 0.0374 |
| 298.15 | 0.0044 | 0.0372 |
| 298.15 | 0.0071 | 0.0367 |
| 298.15 | 0.0117 | 0.0365 |
| 298.15 | 0.0213 | 0.0362 |
| 298.15 | 0.0303 | 0.0360 |
| 298.15 | 0.0492 | 0.0355 |
| 298.15 | 1.0000 | 0.0237 |
| 303.15 | 0.0000 | 0.0381 |
| 303.15 | 0.0034 | 0.0369 |
| 303.15 | 0.0044 | 0.0368 |
| 303.15 | 0.0071 | 0.0362 |
| 303.15 | 0.0117 | 0.0360 |
| 303.15 | 0.0213 | 0.0357 |
| 303.15 | 0.0303 | 0.0355 |
| 303.15 | 0.0492 | 0.0351 |
| 303.15 | 1.0000 | 0.0233 |
| 308.15 | 0.0000 | 0.0376 |
| 308.15 | 0.0034 | 0.0365 |
| 308.15 | 0.0044 | 0.0364 |
| 308.15 | 0.0071 | 0.0358 |
| 308.15 | 0.0117 | 0.0356 |
| 308.15 | 0.0213 | 0.0352 |
| 308.15 | 0.0303 | 0.0350 |
| 308.15 | 0.0492 | 0.0346 |
| 308.15 | 1.0000 | 0.0228 |
| 313.15 | 0.0000 | 0.0372 |
| 313.15 | 0.0034 | 0.0361 |
| 313.15 | 0.0044 | 0.0359 |
| 313.15 | 0.0071 | 0.0353 |
| 313.15 | 0.0117 | 0.0351 |
| 313.15 | 0.0213 | 0.0347 |
| 313.15 | 0.0303 | 0.0346 |
| 313.15 | 0.0492 | 0.0342 |
| 313.15 | 1.0000 | 0.0224 |
| 318.15 | 0.0000 | 0.0366 |
| 318.15 | 0.0034 | 0.0356 |
| 318.15 | 0.0044 | 0.0355 |
| 318.15 | 0.0071 | 0.0348 |
| 318.15 | 0.0117 | 0.0347 |
| 318.15 | 0.0213 | 0.0343 |
| 318.15 | 0.0303 | 0.0340 |
| 318.15 | 0.0492 | 0.0337 |
| 318.15 | 1.0000 | 0.0220 |
| 323.15 | 0.0000 | 0.0362 |
| 323.15 | 0.0034 | 0.0352 |
| 323.15 | 0.0044 | 0.0351 |
| 323.15 | 0.0071 | 0.0344 |
| 323.15 | 0.0117 | 0.0342 |
| 323.15 | 0.0213 | 0.0338 |
| 323.15 | 0.0303 | 0.0336 |
| 323.15 | 0.0492 | 0.0333 |
| 323.15 | 1.0000 | 0.0215 |