Datasets
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Mole fraction (8)
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Binary diffusion coefficient, m2/s (2)
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Partial molar volume, m3/mol (2)
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 2 |
308.15 |
101.30 |
0.5820 |
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 2 |
308.15 |
101.00 |
0.5820 |
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 1 |
308.15 |
101.00 |
0.0040 |
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 1 |
333.15 |
0.0051 |
343.15 |
0.0056 |
353.15 |
0.0055 |
363.15 |
0.0065 |
373.10 |
0.0065 |
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 2 |
308.15 |
101.30 |
0.5820 |
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 2 |
308.15 |
101.00 |
0.5820 |
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 1 |
308.15 |
101.00 |
0.0040 |
Mole fraction of Phenylethyl Alcohol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Phenylethyl Alcohol (1) - Liquid mixture 1 |
333.15 |
0.0051 |
343.15 |
0.0056 |
353.15 |
0.0055 |
363.15 |
0.0065 |
373.10 |
0.0065 |
Binary diffusion coefficient, m2/s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Phenylethyl Alcohol (1) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.15 |
101.00 |
0.0000 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Phenylethyl Alcohol (1) - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.15 |
101.00 |
0.0000 |
0.0000 |
Partial molar volume, m3/mol of Phenylethyl Alcohol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Partial molar volume, m3/mol of Phenylethyl Alcohol (1) - Liquid |
298.14 |
450.00 |
0.0001 |
298.15 |
16010.00 |
0.0001 |
298.16 |
30020.00 |
0.0001 |
318.14 |
490.00 |
0.0001 |
318.14 |
15360.00 |
0.0001 |
318.15 |
29970.00 |
0.0001 |
338.16 |
510.00 |
0.0001 |
338.16 |
15060.00 |
0.0001 |
338.16 |
30090.00 |
0.0001 |
373.15 |
14970.00 |
0.0001 |
373.15 |
30250.00 |
0.0001 |
373.16 |
1950.00 |
0.0001 |
408.15 |
2300.00 |
0.0001 |
408.15 |
14940.00 |
0.0001 |
408.15 |
30400.00 |
0.0001 |
443.16 |
2040.00 |
0.0001 |
443.17 |
15130.00 |
0.0001 |
443.17 |
30390.00 |
0.0001 |
473.16 |
2170.00 |
0.0001 |
473.16 |
16080.00 |
0.0001 |
473.16 |
30250.00 |
0.0001 |
498.62 |
3830.00 |
0.0002 |
498.62 |
16120.00 |
0.0002 |
498.68 |
30260.00 |
0.0001 |
523.15 |
7080.00 |
0.0002 |
523.15 |
18170.00 |
0.0002 |
523.15 |
30310.00 |
0.0002 |
548.18 |
10410.00 |
0.0002 |
548.18 |
19250.00 |
0.0002 |
548.18 |
30330.00 |
0.0002 |
573.15 |
10410.00 |
0.0002 |
573.15 |
30760.00 |
0.0002 |
573.16 |
13390.00 |
0.0002 |
573.16 |
21250.00 |
0.0002 |
573.17 |
25080.00 |
0.0002 |
Partial molar volume, m3/mol of Phenylethyl Alcohol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Partial molar volume, m3/mol of Phenylethyl Alcohol (1) - Liquid |
298.14 |
450.00 |
0.0001 |
298.15 |
16010.00 |
0.0001 |
298.16 |
30020.00 |
0.0001 |
318.14 |
490.00 |
0.0001 |
318.14 |
15360.00 |
0.0001 |
318.15 |
29970.00 |
0.0001 |
338.16 |
510.00 |
0.0001 |
338.16 |
15060.00 |
0.0001 |
338.16 |
30090.00 |
0.0001 |
373.15 |
14970.00 |
0.0001 |
373.15 |
30250.00 |
0.0001 |
373.16 |
1950.00 |
0.0001 |
408.15 |
2300.00 |
0.0001 |
408.15 |
14940.00 |
0.0001 |
408.15 |
30400.00 |
0.0001 |
443.16 |
2040.00 |
0.0001 |
443.17 |
15130.00 |
0.0001 |
443.17 |
30390.00 |
0.0001 |
473.16 |
2170.00 |
0.0001 |
473.16 |
16080.00 |
0.0001 |
473.16 |
30250.00 |
0.0001 |
498.62 |
3830.00 |
0.0002 |
498.62 |
16120.00 |
0.0002 |
498.68 |
30260.00 |
0.0001 |
523.15 |
7080.00 |
0.0002 |
523.15 |
18170.00 |
0.0002 |
523.15 |
30310.00 |
0.0002 |
548.18 |
10410.00 |
0.0002 |
548.18 |
19250.00 |
0.0002 |
548.18 |
30330.00 |
0.0002 |
573.15 |
10410.00 |
0.0002 |
573.15 |
30760.00 |
0.0002 |
573.16 |
13390.00 |
0.0002 |
573.16 |
21250.00 |
0.0002 |
573.17 |
25080.00 |
0.0002 |
Sources