Mixture of Propane, 2-methoxy-2-methyl- + Phenol + Water

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Propane, 2-methoxy-2-methyl-

Name
Propane, 2-methoxy-2-methyl-
InChI
InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
InChI Key
BZLVMXJERCGZMT-UHFFFAOYSA-N
Formula
C5H12O
SMILES
COC(C)(C)C
Mol. Weight (g/mol)
88.15
CAS
1634-04-4

Phenol

Name
Phenol
InChI
InChI=1S/C6H6O/c7-6-4-2-1-3-5-6/h1-5,7H
InChI Key
ISWSIDIOOBJBQZ-UHFFFAOYSA-N
Formula
C6H6O
SMILES
Oc1ccccc1
Mol. Weight (g/mol)
94.11
CAS
108-95-2

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
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Datasets

  1. Temperature, K x Mass fraction (2)

Temperature, K x Mass fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 Mass fraction of Phenol (2) - Liquid mixture 1 Mass fraction of Phenol (2) - Liquid mixture 2 Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2
298.15 0.8991 0.0588 0.0011 0.0251
298.15 0.9252 0.0441 0.0009 0.0253
298.15 0.9334 0.0399 0.0007 0.0258
298.15 0.9435 0.0332 0.0006 0.0262
298.15 0.9479 0.0313 0.0006 0.0262
298.15 0.9523 0.0284 0.0006 0.0265
298.15 0.9551 0.0266 0.0005 0.0267
298.15 0.9601 0.0229 0.0004 0.0275
298.15 0.9645 0.0202 0.0004 0.0291
298.15 0.9661 0.0194 0.0003 0.0299
298.15 0.9692 0.0175 0.0003 0.0303
298.15 0.9798 0.0070 0.0001 0.0304
298.15 0.9826 0.0047 0.0001 0.0315
298.15 0.9875 0.0000 0.0000 0.0329
313.15 0.8263 0.1242 0.0025 0.0181
313.15 0.8482 0.1087 0.0024 0.0192
313.15 0.8635 0.0979 0.0019 0.0193
313.15 0.8842 0.0790 0.0016 0.0207
313.15 0.8896 0.0747 0.0015 0.0208
313.15 0.8955 0.0698 0.0014 0.0210
313.15 0.9281 0.0456 0.0009 0.0215
313.15 0.9325 0.0420 0.0008 0.0234
313.15 0.9498 0.0293 0.0007 0.0240
313.15 0.9584 0.0241 0.0004 0.0241
313.15 0.9673 0.0163 0.0003 0.0245
313.15 0.9807 0.0038 0.0001 0.0248
313.15 0.9819 0.0027 0.0001 0.0248
313.15 0.9853 0.0000 0.0000 0.0250
323.15 0.8935 0.0685 0.0017 0.0124
323.15 0.9012 0.0634 0.0017 0.0132
323.15 0.9316 0.0393 0.0010 0.0143
323.15 0.9365 0.0352 0.0009 0.0147
323.15 0.9506 0.0264 0.0006 0.0149
323.15 0.9558 0.0214 0.0005 0.0150
323.15 0.9578 0.0202 0.0005 0.0152
323.15 0.9636 0.0160 0.0004 0.0152
323.15 0.9666 0.0139 0.0004 0.0161
323.15 0.9690 0.0123 0.0003 0.0163
323.15 0.9738 0.0089 0.0002 0.0164
323.15 0.9754 0.0083 0.0002 0.0170
323.15 0.9808 0.0032 0.0001 0.0176
323.15 0.9842 0.0000 0.0000 0.0190

Temperature, K x Mass fraction [ref]

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

Fixed Measured
Temperature, K - Liquid mixture 2 Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 Mass fraction of Phenol (2) - Liquid mixture 1 Mass fraction of Phenol (2) - Liquid mixture 2 Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2
298.15 0.8991 0.0588 0.0011 0.0251
298.15 0.9252 0.0441 0.0009 0.0253
298.15 0.9334 0.0399 0.0007 0.0258
298.15 0.9435 0.0332 0.0006 0.0262
298.15 0.9479 0.0313 0.0006 0.0262
298.15 0.9523 0.0284 0.0006 0.0265
298.15 0.9551 0.0266 0.0005 0.0267
298.15 0.9601 0.0229 0.0004 0.0275
298.15 0.9645 0.0202 0.0004 0.0291
298.15 0.9661 0.0194 0.0003 0.0299
298.15 0.9692 0.0175 0.0003 0.0303
298.15 0.9798 0.0070 0.0001 0.0304
298.15 0.9826 0.0047 0.0001 0.0315
298.15 0.9875 0.0000 0.0000 0.0329
313.15 0.8263 0.1242 0.0025 0.0181
313.15 0.8482 0.1087 0.0024 0.0192
313.15 0.8635 0.0979 0.0019 0.0193
313.15 0.8842 0.0790 0.0016 0.0207
313.15 0.8896 0.0747 0.0015 0.0208
313.15 0.8955 0.0698 0.0014 0.0210
313.15 0.9281 0.0456 0.0009 0.0215
313.15 0.9325 0.0420 0.0008 0.0234
313.15 0.9498 0.0293 0.0007 0.0240
313.15 0.9584 0.0241 0.0004 0.0241
313.15 0.9673 0.0163 0.0003 0.0245
313.15 0.9807 0.0038 0.0001 0.0248
313.15 0.9819 0.0027 0.0001 0.0248
313.15 0.9853 0.0000 0.0000 0.0250
323.15 0.8935 0.0685 0.0017 0.0124
323.15 0.9012 0.0634 0.0017 0.0132
323.15 0.9316 0.0393 0.0010 0.0143
323.15 0.9365 0.0352 0.0009 0.0147
323.15 0.9506 0.0264 0.0006 0.0149
323.15 0.9558 0.0214 0.0005 0.0150
323.15 0.9578 0.0202 0.0005 0.0152
323.15 0.9636 0.0160 0.0004 0.0152
323.15 0.9666 0.0139 0.0004 0.0161
323.15 0.9690 0.0123 0.0003 0.0163
323.15 0.9738 0.0089 0.0002 0.0164
323.15 0.9754 0.0083 0.0002 0.0170
323.15 0.9808 0.0032 0.0001 0.0176
323.15 0.9842 0.0000 0.0000 0.0190

Sources