Mixture of Methyl Isobutyl Ketone + 1,2-Benzenediol + Water

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Methyl Isobutyl Ketone

Name
Methyl Isobutyl Ketone
InChI
InChI=1S/C6H12O/c1-5(2)4-6(3)7/h5H,4H2,1-3H3
InChI Key
NTIZESTWPVYFNL-UHFFFAOYSA-N
Formula
C6H12O
SMILES
CC(=O)CC(C)C
Mol. Weight (g/mol)
100.16
CAS
108-10-1

1,2-Benzenediol

Name
1,2-Benzenediol
InChI
InChI=1S/C6H6O2/c7-5-3-1-2-4-6(5)8/h1-4,7-8H
InChI Key
YCIMNLLNPGFGHC-UHFFFAOYSA-N
Formula
C6H6O2
SMILES
Oc1ccccc1O
Mol. Weight (g/mol)
110.11
CAS
120-80-9

Water

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

Datasets

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 2
318.15 0.1884 0.7433 0.0121 0.0150
318.15 0.2051 0.7202 0.0118 0.0183
318.15 0.2485 0.6586 0.0113 0.0293
318.15 0.2842 0.6064 0.0103 0.0345
318.15 0.3188 0.5608 0.0096 0.0417
318.15 0.3477 0.5201 0.0093 0.0487
318.15 0.3658 0.4933 0.0091 0.0551
318.15 0.3819 0.4603 0.0090 0.0589
318.15 0.3945 0.4396 0.0089 0.0636
298.15 0.0000 0.9802 0.0190 0.0000
298.15 0.0004 0.9796 0.0182 0.0001
298.15 0.0006 0.9788 0.0181 0.0001
298.15 0.0019 0.9779 0.0178 0.0001
298.15 0.0081 0.9707 0.0167 0.0003
298.15 0.0192 0.9576 0.0163 0.0007
298.15 0.0430 0.9311 0.0161 0.0017
298.15 0.0866 0.8834 0.0161 0.0042
298.15 0.1483 0.8115 0.0155 0.0088
298.15 0.1864 0.7557 0.0154 0.0123
298.15 0.2214 0.7263 0.0151 0.0158
298.15 0.2618 0.6731 0.0131 0.0207
298.15 0.2997 0.6158 0.0119 0.0285
298.15 0.3342 0.5753 0.0111 0.0354
298.15 0.3605 0.5350 0.0113 0.0397
298.15 0.3957 0.4854 0.0109 0.0452
298.15 0.4279 0.4387 0.0101 0.0491
298.15 0.4360 0.4058 0.0099 0.0513
308.15 0.0000 0.9762 0.0169 0.0000
308.15 0.0006 0.9746 0.0169 0.0001
308.15 0.0010 0.9741 0.0168 0.0001
308.15 0.0025 0.9724 0.0166 0.0001
308.15 0.0072 0.9671 0.0162 0.0003
308.15 0.0202 0.9524 0.0160 0.0009
308.15 0.0429 0.9266 0.0153 0.0022
308.15 0.0905 0.8713 0.0159 0.0051
308.15 0.1541 0.7966 0.0132 0.0099
308.15 0.1872 0.7562 0.0131 0.0137
308.15 0.2104 0.7199 0.0127 0.0160
308.15 0.2587 0.6557 0.0122 0.0217
308.15 0.2945 0.6072 0.0111 0.0303
308.15 0.3321 0.5583 0.0109 0.0387
308.15 0.3518 0.5309 0.0109 0.0433
308.15 0.3789 0.4919 0.0108 0.0492
308.15 0.3946 0.4688 0.0103 0.0526
308.15 0.4124 0.4375 0.0099 0.0561
318.15 0.0000 0.9722 0.0152 0.0000
318.15 0.0002 0.9722 0.0149 0.0001
318.15 0.0005 0.9721 0.0148 0.0001
318.15 0.0012 0.9713 0.0147 0.0001
318.15 0.0079 0.9635 0.0145 0.0004
318.15 0.0197 0.9502 0.0137 0.0010
318.15 0.0435 0.9223 0.0132 0.0025
318.15 0.0878 0.8696 0.0131 0.0058
318.15 0.1486 0.7965 0.0124 0.0113

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 2
318.15 0.1884 0.7433 0.0121 0.0150
318.15 0.2051 0.7202 0.0118 0.0183
318.15 0.2485 0.6586 0.0113 0.0293
318.15 0.2842 0.6064 0.0103 0.0345
318.15 0.3188 0.5608 0.0096 0.0417
318.15 0.3477 0.5201 0.0093 0.0487
318.15 0.3658 0.4933 0.0091 0.0551
318.15 0.3819 0.4603 0.0090 0.0589
318.15 0.3945 0.4396 0.0089 0.0636
298.15 0.0000 0.9802 0.0190 0.0000
298.15 0.0004 0.9796 0.0182 0.0001
298.15 0.0006 0.9788 0.0181 0.0001
298.15 0.0019 0.9779 0.0178 0.0001
298.15 0.0081 0.9707 0.0167 0.0003
298.15 0.0192 0.9576 0.0163 0.0007
298.15 0.0430 0.9311 0.0161 0.0017
298.15 0.0866 0.8834 0.0161 0.0042
298.15 0.1483 0.8115 0.0155 0.0088
298.15 0.1864 0.7557 0.0154 0.0123
298.15 0.2214 0.7263 0.0151 0.0158
298.15 0.2618 0.6731 0.0131 0.0207
298.15 0.2997 0.6158 0.0119 0.0285
298.15 0.3342 0.5753 0.0111 0.0354
298.15 0.3605 0.5350 0.0113 0.0397
298.15 0.3957 0.4854 0.0109 0.0452
298.15 0.4279 0.4387 0.0101 0.0491
298.15 0.4360 0.4058 0.0099 0.0513
308.15 0.0000 0.9762 0.0169 0.0000
308.15 0.0006 0.9746 0.0169 0.0001
308.15 0.0010 0.9741 0.0168 0.0001
308.15 0.0025 0.9724 0.0166 0.0001
308.15 0.0072 0.9671 0.0162 0.0003
308.15 0.0202 0.9524 0.0160 0.0009
308.15 0.0429 0.9266 0.0153 0.0022
308.15 0.0905 0.8713 0.0159 0.0051
308.15 0.1541 0.7966 0.0132 0.0099
308.15 0.1872 0.7562 0.0131 0.0137
308.15 0.2104 0.7199 0.0127 0.0160
308.15 0.2587 0.6557 0.0122 0.0217
308.15 0.2945 0.6072 0.0111 0.0303
308.15 0.3321 0.5583 0.0109 0.0387
308.15 0.3518 0.5309 0.0109 0.0433
308.15 0.3789 0.4919 0.0108 0.0492
308.15 0.3946 0.4688 0.0103 0.0526
308.15 0.4124 0.4375 0.0099 0.0561
318.15 0.0000 0.9722 0.0152 0.0000
318.15 0.0002 0.9722 0.0149 0.0001
318.15 0.0005 0.9721 0.0148 0.0001
318.15 0.0012 0.9713 0.0147 0.0001
318.15 0.0079 0.9635 0.0145 0.0004
318.15 0.0197 0.9502 0.0137 0.0010
318.15 0.0435 0.9223 0.0132 0.0025
318.15 0.0878 0.8696 0.0131 0.0058
318.15 0.1486 0.7965 0.0124 0.0113

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 2
318.15 0.1884 0.7433 0.0121 0.0150
318.15 0.2051 0.7202 0.0118 0.0183
318.15 0.2485 0.6586 0.0113 0.0293
318.15 0.2842 0.6064 0.0103 0.0345
318.15 0.3188 0.5608 0.0096 0.0417
318.15 0.3477 0.5201 0.0093 0.0487
318.15 0.3658 0.4933 0.0091 0.0551
318.15 0.3819 0.4603 0.0090 0.0589
318.15 0.3945 0.4396 0.0089 0.0636
298.15 0.0000 0.9802 0.0190 0.0000
298.15 0.0004 0.9796 0.0182 0.0001
298.15 0.0006 0.9788 0.0181 0.0001
298.15 0.0019 0.9779 0.0178 0.0001
298.15 0.0081 0.9707 0.0167 0.0003
298.15 0.0192 0.9576 0.0163 0.0007
298.15 0.0430 0.9311 0.0161 0.0017
298.15 0.0866 0.8834 0.0161 0.0042
298.15 0.1483 0.8115 0.0155 0.0088
298.15 0.1864 0.7557 0.0154 0.0123
298.15 0.2214 0.7263 0.0151 0.0158
298.15 0.2618 0.6731 0.0131 0.0207
298.15 0.2997 0.6158 0.0119 0.0285
298.15 0.3342 0.5753 0.0111 0.0354
298.15 0.3605 0.5350 0.0113 0.0397
298.15 0.3957 0.4854 0.0109 0.0452
298.15 0.4279 0.4387 0.0101 0.0491
298.15 0.4360 0.4058 0.0099 0.0513
308.15 0.0000 0.9762 0.0169 0.0000
308.15 0.0006 0.9746 0.0169 0.0001
308.15 0.0010 0.9741 0.0168 0.0001
308.15 0.0025 0.9724 0.0166 0.0001
308.15 0.0072 0.9671 0.0162 0.0003
308.15 0.0202 0.9524 0.0160 0.0009
308.15 0.0429 0.9266 0.0153 0.0022
308.15 0.0905 0.8713 0.0159 0.0051
308.15 0.1541 0.7966 0.0132 0.0099
308.15 0.1872 0.7562 0.0131 0.0137
308.15 0.2104 0.7199 0.0127 0.0160
308.15 0.2587 0.6557 0.0122 0.0217
308.15 0.2945 0.6072 0.0111 0.0303
308.15 0.3321 0.5583 0.0109 0.0387
308.15 0.3518 0.5309 0.0109 0.0433
308.15 0.3789 0.4919 0.0108 0.0492
308.15 0.3946 0.4688 0.0103 0.0526
308.15 0.4124 0.4375 0.0099 0.0561
318.15 0.0000 0.9722 0.0152 0.0000
318.15 0.0002 0.9722 0.0149 0.0001
318.15 0.0005 0.9721 0.0148 0.0001
318.15 0.0012 0.9713 0.0147 0.0001
318.15 0.0079 0.9635 0.0145 0.0004
318.15 0.0197 0.9502 0.0137 0.0010
318.15 0.0435 0.9223 0.0132 0.0025
318.15 0.0878 0.8696 0.0131 0.0058
318.15 0.1486 0.7965 0.0124 0.0113

Temperature, K x Mass fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mass fraction of 1,2-Benzenediol (2) - Liquid mixture 2
318.15 0.1884 0.7433 0.0121 0.0150
318.15 0.2051 0.7202 0.0118 0.0183
318.15 0.2485 0.6586 0.0113 0.0293
318.15 0.2842 0.6064 0.0103 0.0345
318.15 0.3188 0.5608 0.0096 0.0417
318.15 0.3477 0.5201 0.0093 0.0487
318.15 0.3658 0.4933 0.0091 0.0551
318.15 0.3819 0.4603 0.0090 0.0589
318.15 0.3945 0.4396 0.0089 0.0636
298.15 0.0000 0.9802 0.0190 0.0000
298.15 0.0004 0.9796 0.0182 0.0001
298.15 0.0006 0.9788 0.0181 0.0001
298.15 0.0019 0.9779 0.0178 0.0001
298.15 0.0081 0.9707 0.0167 0.0003
298.15 0.0192 0.9576 0.0163 0.0007
298.15 0.0430 0.9311 0.0161 0.0017
298.15 0.0866 0.8834 0.0161 0.0042
298.15 0.1483 0.8115 0.0155 0.0088
298.15 0.1864 0.7557 0.0154 0.0123
298.15 0.2214 0.7263 0.0151 0.0158
298.15 0.2618 0.6731 0.0131 0.0207
298.15 0.2997 0.6158 0.0119 0.0285
298.15 0.3342 0.5753 0.0111 0.0354
298.15 0.3605 0.5350 0.0113 0.0397
298.15 0.3957 0.4854 0.0109 0.0452
298.15 0.4279 0.4387 0.0101 0.0491
298.15 0.4360 0.4058 0.0099 0.0513
308.15 0.0000 0.9762 0.0169 0.0000
308.15 0.0006 0.9746 0.0169 0.0001
308.15 0.0010 0.9741 0.0168 0.0001
308.15 0.0025 0.9724 0.0166 0.0001
308.15 0.0072 0.9671 0.0162 0.0003
308.15 0.0202 0.9524 0.0160 0.0009
308.15 0.0429 0.9266 0.0153 0.0022
308.15 0.0905 0.8713 0.0159 0.0051
308.15 0.1541 0.7966 0.0132 0.0099
308.15 0.1872 0.7562 0.0131 0.0137
308.15 0.2104 0.7199 0.0127 0.0160
308.15 0.2587 0.6557 0.0122 0.0217
308.15 0.2945 0.6072 0.0111 0.0303
308.15 0.3321 0.5583 0.0109 0.0387
308.15 0.3518 0.5309 0.0109 0.0433
308.15 0.3789 0.4919 0.0108 0.0492
308.15 0.3946 0.4688 0.0103 0.0526
308.15 0.4124 0.4375 0.0099 0.0561
318.15 0.0000 0.9722 0.0152 0.0000
318.15 0.0002 0.9722 0.0149 0.0001
318.15 0.0005 0.9721 0.0148 0.0001
318.15 0.0012 0.9713 0.0147 0.0001
318.15 0.0079 0.9635 0.0145 0.0004
318.15 0.0197 0.9502 0.0137 0.0010
318.15 0.0435 0.9223 0.0132 0.0025
318.15 0.0878 0.8696 0.0131 0.0058
318.15 0.1486 0.7965 0.0124 0.0113

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