Mixture of Methyl Isobutyl Ketone + Resorcinol + Water

Excel

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

Resorcinol

Name
Resorcinol
InChI
InChI=1S/C6H6O2/c7-5-2-1-3-6(8)4-5/h1-4,7-8H
InChI Key
GHMLBKRAJCXXBS-UHFFFAOYSA-N
Formula
C6H6O2
SMILES
Oc1cccc(O)c1
Mol. Weight (g/mol)
110.11
CAS
108-46-3

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Temperature, K x Mole fraction (4)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Resorcinol (2) - Liquid mixture 2 Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mole fraction of Resorcinol (2) - Liquid mixture 1 Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1
333.15 0.0034 0.0010 0.1470 0.4106
333.15 0.0026 0.0010 0.1238 0.4722
333.15 0.0023 0.0012 0.1130 0.5004
333.15 0.0020 0.0012 0.1019 0.5251
333.15 0.0017 0.0014 0.0879 0.5495
333.15 0.0013 0.0016 0.0712 0.5873
333.15 0.0010 0.0017 0.0602 0.6197
333.15 0.0007 0.0018 0.0412 0.6901
333.15 0.0004 0.0019 0.0231 0.7325
333.15 0.0000 0.0023 0.0000 0.8109
343.15 0.0039 0.0010 0.1509 0.3796
343.15 0.0031 0.0010 0.1320 0.4310
343.15 0.0028 0.0011 0.1216 0.4606
343.15 0.0024 0.0012 0.1087 0.4837
343.15 0.0020 0.0014 0.0960 0.5083
343.15 0.0018 0.0015 0.0869 0.5333
343.15 0.0012 0.0017 0.0616 0.5849
343.15 0.0007 0.0018 0.0412 0.6494
343.15 0.0005 0.0019 0.0284 0.6808
343.15 0.0000 0.0022 0.0000 0.7410
353.15 0.0041 0.0009 0.1519 0.3752
353.15 0.0034 0.0010 0.1303 0.4114
353.15 0.0030 0.0011 0.1189 0.4406
353.15 0.0027 0.0012 0.1078 0.4572
353.15 0.0023 0.0014 0.0967 0.4865
353.15 0.0020 0.0015 0.0904 0.5131
353.15 0.0015 0.0016 0.0675 0.5597
353.15 0.0008 0.0017 0.0438 0.6140
353.15 0.0006 0.0018 0.0307 0.6533
353.15 0.0000 0.0019 0.0000 0.6924

Temperature, K x Mass fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Resorcinol (2) - Liquid mixture 2 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 Mass fraction of Resorcinol (2) - Liquid mixture 1
298.15 0.0000 0.0181 0.9802 0.0000
308.15 0.0005 0.0157 0.9645 0.0107
308.15 0.0017 0.0155 0.9387 0.0337
298.15 0.0001 0.0180 0.9766 0.0032
308.15 0.0046 0.0150 0.8979 0.0693
308.15 0.0099 0.0144 0.8463 0.1155
308.15 0.0136 0.0142 0.8095 0.1487
308.15 0.0256 0.0139 0.7548 0.1940
308.15 0.0474 0.0140 0.6665 0.2670
308.15 0.0777 0.0149 0.5949 0.3207
308.15 0.1220 0.0154 0.5013 0.3899
298.15 0.0475 0.0154 0.6489 0.2779
308.15 0.1635 0.0180 0.4339 0.4330
308.15 0.2130 0.0239 0.3517 0.4730
318.15 0.0000 0.0146 0.9766 0.0000
298.15 0.0002 0.0179 0.9730 0.0057
318.15 0.0001 0.0146 0.9740 0.0024
318.15 0.0003 0.0145 0.9707 0.0053
318.15 0.0007 0.0144 0.9633 0.0121
318.15 0.0023 0.0142 0.9365 0.0354
318.15 0.0049 0.0138 0.9036 0.0645
318.15 0.0116 0.0134 0.8421 0.1186
298.15 0.0809 0.0166 0.5618 0.3408
318.15 0.0205 0.0131 0.7949 0.1586
318.15 0.0260 0.0130 0.7616 0.1868
318.15 0.0449 0.0131 0.6903 0.2461
318.15 0.0807 0.0141 0.5955 0.3214
298.15 0.0004 0.0179 0.9653 0.0111
318.15 0.1386 0.0165 0.4885 0.3974
318.15 0.1799 0.0189 0.4176 0.4405
318.15 0.2171 0.0222 0.3710 0.4572
298.15 0.0014 0.0175 0.9408 0.0327
298.15 0.0040 0.0169 0.8959 0.0726
298.15 0.1508 0.0185 0.4341 0.4323
298.15 0.0093 0.0162 0.8434 0.1182
298.15 0.0161 0.0157 0.7993 0.1554
298.15 0.0240 0.0154 0.7504 0.1950
298.15 0.1844 0.0212 0.3782 0.4654
298.15 0.2177 0.0267 0.3217 0.4904
308.15 0.0000 0.0159 0.9780 0.0000
308.15 0.0001 0.0159 0.9753 0.0023
308.15 0.0002 0.0159 0.9716 0.0047

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Resorcinol (2) - Liquid mixture 2 Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mole fraction of Resorcinol (2) - Liquid mixture 1 Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1
333.15 0.0034 0.0010 0.1470 0.4106
333.15 0.0026 0.0010 0.1238 0.4722
333.15 0.0023 0.0012 0.1130 0.5004
333.15 0.0020 0.0012 0.1019 0.5251
333.15 0.0017 0.0014 0.0879 0.5495
333.15 0.0013 0.0016 0.0712 0.5873
333.15 0.0010 0.0017 0.0602 0.6197
333.15 0.0007 0.0018 0.0412 0.6901
333.15 0.0004 0.0019 0.0231 0.7325
333.15 0.0000 0.0023 0.0000 0.8109
343.15 0.0039 0.0010 0.1509 0.3796
343.15 0.0031 0.0010 0.1320 0.4310
343.15 0.0028 0.0011 0.1216 0.4606
343.15 0.0024 0.0012 0.1087 0.4837
343.15 0.0020 0.0014 0.0960 0.5083
343.15 0.0018 0.0015 0.0869 0.5333
343.15 0.0012 0.0017 0.0616 0.5849
343.15 0.0007 0.0018 0.0412 0.6494
343.15 0.0005 0.0019 0.0284 0.6808
343.15 0.0000 0.0022 0.0000 0.7410
353.15 0.0041 0.0009 0.1519 0.3752
353.15 0.0034 0.0010 0.1303 0.4114
353.15 0.0030 0.0011 0.1189 0.4406
353.15 0.0027 0.0012 0.1078 0.4572
353.15 0.0023 0.0014 0.0967 0.4865
353.15 0.0020 0.0015 0.0904 0.5131
353.15 0.0015 0.0016 0.0675 0.5597
353.15 0.0008 0.0017 0.0438 0.6140
353.15 0.0006 0.0018 0.0307 0.6533
353.15 0.0000 0.0019 0.0000 0.6924

Temperature, K x Mass fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 1 Mass fraction of Resorcinol (2) - Liquid mixture 2 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 Mass fraction of Resorcinol (2) - Liquid mixture 1
298.15 0.0000 0.0181 0.9802 0.0000
308.15 0.0005 0.0157 0.9645 0.0107
308.15 0.0017 0.0155 0.9387 0.0337
298.15 0.0001 0.0180 0.9766 0.0032
308.15 0.0046 0.0150 0.8979 0.0693
308.15 0.0099 0.0144 0.8463 0.1155
308.15 0.0136 0.0142 0.8095 0.1487
308.15 0.0256 0.0139 0.7548 0.1940
308.15 0.0474 0.0140 0.6665 0.2670
308.15 0.0777 0.0149 0.5949 0.3207
308.15 0.1220 0.0154 0.5013 0.3899
298.15 0.0475 0.0154 0.6489 0.2779
308.15 0.1635 0.0180 0.4339 0.4330
308.15 0.2130 0.0239 0.3517 0.4730
318.15 0.0000 0.0146 0.9766 0.0000
298.15 0.0002 0.0179 0.9730 0.0057
318.15 0.0001 0.0146 0.9740 0.0024
318.15 0.0003 0.0145 0.9707 0.0053
318.15 0.0007 0.0144 0.9633 0.0121
318.15 0.0023 0.0142 0.9365 0.0354
318.15 0.0049 0.0138 0.9036 0.0645
318.15 0.0116 0.0134 0.8421 0.1186
298.15 0.0809 0.0166 0.5618 0.3408
318.15 0.0205 0.0131 0.7949 0.1586
318.15 0.0260 0.0130 0.7616 0.1868
318.15 0.0449 0.0131 0.6903 0.2461
318.15 0.0807 0.0141 0.5955 0.3214
298.15 0.0004 0.0179 0.9653 0.0111
318.15 0.1386 0.0165 0.4885 0.3974
318.15 0.1799 0.0189 0.4176 0.4405
318.15 0.2171 0.0222 0.3710 0.4572
298.15 0.0014 0.0175 0.9408 0.0327
298.15 0.0040 0.0169 0.8959 0.0726
298.15 0.1508 0.0185 0.4341 0.4323
298.15 0.0093 0.0162 0.8434 0.1182
298.15 0.0161 0.0157 0.7993 0.1554
298.15 0.0240 0.0154 0.7504 0.1950
298.15 0.1844 0.0212 0.3782 0.4654
298.15 0.2177 0.0267 0.3217 0.4904
308.15 0.0000 0.0159 0.9780 0.0000
308.15 0.0001 0.0159 0.9753 0.0023
308.15 0.0002 0.0159 0.9716 0.0047

Sources