Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 2 | Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 333.15 | 0.0007 | 0.0009 | 0.3989 | 0.2413 |
| 333.15 | 0.0009 | 0.0008 | 0.3563 | 0.3010 |
| 333.15 | 0.0010 | 0.0007 | 0.3318 | 0.3391 |
| 333.15 | 0.0011 | 0.0006 | 0.2865 | 0.3971 |
| 333.15 | 0.0013 | 0.0005 | 0.2365 | 0.4566 |
| 333.15 | 0.0014 | 0.0004 | 0.2102 | 0.4929 |
| 333.15 | 0.0015 | 0.0003 | 0.1886 | 0.5293 |
| 333.15 | 0.0016 | 0.0002 | 0.1433 | 0.5864 |
| 333.15 | 0.0018 | 0.0001 | 0.1007 | 0.6361 |
| 333.15 | 0.0023 | 0.0000 | 0.0000 | 0.8112 |
| 343.15 | 0.0007 | 0.0010 | 0.4042 | 0.2263 |
| 343.15 | 0.0008 | 0.0008 | 0.3529 | 0.2805 |
| 343.15 | 0.0009 | 0.0007 | 0.3267 | 0.3178 |
| 343.15 | 0.0011 | 0.0006 | 0.2846 | 0.3702 |
| 343.15 | 0.0013 | 0.0005 | 0.2397 | 0.4277 |
| 343.15 | 0.0013 | 0.0004 | 0.2126 | 0.4628 |
| 343.15 | 0.0014 | 0.0003 | 0.1859 | 0.5030 |
| 343.15 | 0.0015 | 0.0002 | 0.1492 | 0.5577 |
| 343.15 | 0.0017 | 0.0002 | 0.1063 | 0.6188 |
| 343.15 | 0.0022 | 0.0000 | 0.0000 | 0.7413 |
| 353.15 | 0.0006 | 0.0010 | 0.4011 | 0.2210 |
| 353.15 | 0.0008 | 0.0009 | 0.3500 | 0.2786 |
| 353.15 | 0.0009 | 0.0008 | 0.3277 | 0.3073 |
| 353.15 | 0.0010 | 0.0007 | 0.2931 | 0.3573 |
| 353.15 | 0.0012 | 0.0005 | 0.2420 | 0.4181 |
| 353.15 | 0.0013 | 0.0005 | 0.2157 | 0.4575 |
| 353.15 | 0.0014 | 0.0004 | 0.1851 | 0.4950 |
| 353.15 | 0.0015 | 0.0003 | 0.1470 | 0.5379 |
| 353.15 | 0.0016 | 0.0002 | 0.1029 | 0.5865 |
| 353.15 | 0.0019 | 0.0000 | 0.0000 | 0.6928 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 1 | Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.20 | 0.0040 | 0.0043 | 0.5283 | 0.4083 |
| 323.20 | 0.0057 | 0.0031 | 0.3927 | 0.5341 |
| 323.20 | 0.0065 | 0.0024 | 0.3347 | 0.5985 |
| 298.20 | 0.0097 | 0.0009 | 0.2078 | 0.7542 |
| 323.20 | 0.0074 | 0.0019 | 0.2858 | 0.6525 |
| 323.20 | 0.0092 | 0.0009 | 0.1855 | 0.7696 |
| 313.20 | 0.0036 | 0.0047 | 0.5425 | 0.3856 |
| 323.20 | 0.0136 | 0.0000 | 0.0000 | 0.9722 |
| 298.20 | 0.0059 | 0.0028 | 0.4094 | 0.5353 |
| 298.20 | 0.0070 | 0.0021 | 0.3428 | 0.6074 |
| 298.20 | 0.0080 | 0.0016 | 0.2944 | 0.6601 |
| 313.20 | 0.0079 | 0.0015 | 0.2644 | 0.6867 |
| 298.20 | 0.0089 | 0.0012 | 0.2468 | 0.7115 |
| 298.20 | 0.0111 | 0.0005 | 0.1538 | 0.8128 |
| 313.20 | 0.0148 | 0.0000 | 0.0000 | 0.9756 |
| 298.20 | 0.0171 | 0.0000 | 0.0000 | 0.9806 |
| 313.20 | 0.0045 | 0.0040 | 0.4872 | 0.4434 |
| 313.20 | 0.0054 | 0.0032 | 0.4252 | 0.5103 |
| 313.20 | 0.0063 | 0.0024 | 0.3612 | 0.5800 |
| 313.20 | 0.0073 | 0.0018 | 0.3004 | 0.6458 |
| 313.20 | 0.0087 | 0.0011 | 0.2163 | 0.7404 |
| 323.20 | 0.0083 | 0.0013 | 0.2284 | 0.7195 |
| 313.20 | 0.0098 | 0.0007 | 0.1681 | 0.7966 |
| 323.20 | 0.0032 | 0.0050 | 0.5505 | 0.3575 |
| 298.20 | 0.0049 | 0.0035 | 0.4646 | 0.4759 |
| 323.20 | 0.0039 | 0.0044 | 0.5046 | 0.4090 |
| 323.20 | 0.0047 | 0.0037 | 0.4544 | 0.4653 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 2 | Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 333.15 | 0.0007 | 0.0009 | 0.3989 | 0.2413 |
| 333.15 | 0.0009 | 0.0008 | 0.3563 | 0.3010 |
| 333.15 | 0.0010 | 0.0007 | 0.3318 | 0.3391 |
| 333.15 | 0.0011 | 0.0006 | 0.2865 | 0.3971 |
| 333.15 | 0.0013 | 0.0005 | 0.2365 | 0.4566 |
| 333.15 | 0.0014 | 0.0004 | 0.2102 | 0.4929 |
| 333.15 | 0.0015 | 0.0003 | 0.1886 | 0.5293 |
| 333.15 | 0.0016 | 0.0002 | 0.1433 | 0.5864 |
| 333.15 | 0.0018 | 0.0001 | 0.1007 | 0.6361 |
| 333.15 | 0.0023 | 0.0000 | 0.0000 | 0.8112 |
| 343.15 | 0.0007 | 0.0010 | 0.4042 | 0.2263 |
| 343.15 | 0.0008 | 0.0008 | 0.3529 | 0.2805 |
| 343.15 | 0.0009 | 0.0007 | 0.3267 | 0.3178 |
| 343.15 | 0.0011 | 0.0006 | 0.2846 | 0.3702 |
| 343.15 | 0.0013 | 0.0005 | 0.2397 | 0.4277 |
| 343.15 | 0.0013 | 0.0004 | 0.2126 | 0.4628 |
| 343.15 | 0.0014 | 0.0003 | 0.1859 | 0.5030 |
| 343.15 | 0.0015 | 0.0002 | 0.1492 | 0.5577 |
| 343.15 | 0.0017 | 0.0002 | 0.1063 | 0.6188 |
| 343.15 | 0.0022 | 0.0000 | 0.0000 | 0.7413 |
| 353.15 | 0.0006 | 0.0010 | 0.4011 | 0.2210 |
| 353.15 | 0.0008 | 0.0009 | 0.3500 | 0.2786 |
| 353.15 | 0.0009 | 0.0008 | 0.3277 | 0.3073 |
| 353.15 | 0.0010 | 0.0007 | 0.2931 | 0.3573 |
| 353.15 | 0.0012 | 0.0005 | 0.2420 | 0.4181 |
| 353.15 | 0.0013 | 0.0005 | 0.2157 | 0.4575 |
| 353.15 | 0.0014 | 0.0004 | 0.1851 | 0.4950 |
| 353.15 | 0.0015 | 0.0003 | 0.1470 | 0.5379 |
| 353.15 | 0.0016 | 0.0002 | 0.1029 | 0.5865 |
| 353.15 | 0.0019 | 0.0000 | 0.0000 | 0.6928 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 1 | Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.20 | 0.0040 | 0.0043 | 0.5283 | 0.4083 |
| 323.20 | 0.0057 | 0.0031 | 0.3927 | 0.5341 |
| 323.20 | 0.0065 | 0.0024 | 0.3347 | 0.5985 |
| 298.20 | 0.0097 | 0.0009 | 0.2078 | 0.7542 |
| 323.20 | 0.0074 | 0.0019 | 0.2858 | 0.6525 |
| 323.20 | 0.0092 | 0.0009 | 0.1855 | 0.7696 |
| 313.20 | 0.0036 | 0.0047 | 0.5425 | 0.3856 |
| 323.20 | 0.0136 | 0.0000 | 0.0000 | 0.9722 |
| 298.20 | 0.0059 | 0.0028 | 0.4094 | 0.5353 |
| 298.20 | 0.0070 | 0.0021 | 0.3428 | 0.6074 |
| 298.20 | 0.0080 | 0.0016 | 0.2944 | 0.6601 |
| 313.20 | 0.0079 | 0.0015 | 0.2644 | 0.6867 |
| 298.20 | 0.0089 | 0.0012 | 0.2468 | 0.7115 |
| 298.20 | 0.0111 | 0.0005 | 0.1538 | 0.8128 |
| 313.20 | 0.0148 | 0.0000 | 0.0000 | 0.9756 |
| 298.20 | 0.0171 | 0.0000 | 0.0000 | 0.9806 |
| 313.20 | 0.0045 | 0.0040 | 0.4872 | 0.4434 |
| 313.20 | 0.0054 | 0.0032 | 0.4252 | 0.5103 |
| 313.20 | 0.0063 | 0.0024 | 0.3612 | 0.5800 |
| 313.20 | 0.0073 | 0.0018 | 0.3004 | 0.6458 |
| 313.20 | 0.0087 | 0.0011 | 0.2163 | 0.7404 |
| 323.20 | 0.0083 | 0.0013 | 0.2284 | 0.7195 |
| 313.20 | 0.0098 | 0.0007 | 0.1681 | 0.7966 |
| 323.20 | 0.0032 | 0.0050 | 0.5505 | 0.3575 |
| 298.20 | 0.0049 | 0.0035 | 0.4646 | 0.4759 |
| 323.20 | 0.0039 | 0.0044 | 0.5046 | 0.4090 |
| 323.20 | 0.0047 | 0.0037 | 0.4544 | 0.4653 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.