Mixture of 1-Propanol, 2-methyl- + Acetophenone

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1-Propanol, 2-methyl-

Name
1-Propanol, 2-methyl-
InChI
InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3
InChI Key
ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)CO
Mol. Weight (g/mol)
74.12
CAS
78-83-1

Acetophenone

Name
Acetophenone
InChI
InChI=1S/C8H8O/c1-7(9)8-5-3-2-4-6-8/h2-6H,1H3
InChI Key
KWOLFJPFCHCOCG-UHFFFAOYSA-N
Formula
C8H8O
SMILES
CC(=O)c1ccccc1
Mol. Weight (g/mol)
120.15
CAS
98-86-2
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of 1-Propanol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid Mole fraction of 1-Propanol, 2-methyl- (1) - Gas
0.0000 0.0000
0.2960 0.8810
0.3540 0.9210
0.4560 0.9480
0.5570 0.9530
0.6270 0.9640
0.6770 0.9710
0.7160 0.9720
0.7460 0.9770
0.7710 0.9780
0.7910 0.9820
0.8080 0.9840
0.8220 0.9850
0.8550 0.9880
0.8940 0.9900
0.9550 0.9930
1.0000 1.0000

Mole fraction of 1-Propanol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid Mole fraction of 1-Propanol, 2-methyl- (1) - Gas
0.0000 0.0000
0.2960 0.8810
0.3540 0.9210
0.4560 0.9480
0.5570 0.9530
0.6270 0.9640
0.6770 0.9710
0.7160 0.9720
0.7460 0.9770
0.7710 0.9780
0.7910 0.9820
0.8080 0.9840
0.8220 0.9850
0.8550 0.9880
0.8940 0.9900
0.9550 0.9930
1.0000 1.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetophenone (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.20 0.1005 0.6958
298.20 0.2010 1.1021
298.20 0.3010 1.3661
298.20 0.3512 1.4489
298.20 0.4014 1.5109
298.20 0.4516 1.5502
298.20 0.5017 1.5673
298.20 0.5518 1.5614
298.20 0.6016 1.5328
298.20 0.6513 1.4795
298.20 0.7008 1.4005
298.20 0.8016 1.1346
298.20 0.9010 0.6842
313.20 0.1005 0.8039
313.20 0.2010 1.3046
313.20 0.3010 1.63
313.20 0.3512 1.732
313.20 0.4014 1.8068
313.20 0.4516 1.8517
313.20 0.5017 1.8663
313.20 0.5518 1.8521
313.20 0.6016 1.8084
313.20 0.6513 1.7354
313.20 0.7008 1.626
313.20 0.8016 1.2766
313.20 0.9010 0.7414
328.20 0.1005 0.9176
328.20 0.2010 1.4909
328.20 0.3010 1.8798
328.20 0.3512 1.9901
328.20 0.4014 2.0685
328.20 0.4516 2.1068
328.20 0.5017 2.1136
328.20 0.5518 2.0832
328.20 0.6016 2.0162
328.20 0.6513 1.9069
328.20 0.7008 1.7708
328.20 0.8016 1.3564
328.20 0.9010 0.7646
338.20 0.1005 0.9335
338.20 0.2010 1.5373
338.20 0.3010 1.9258
338.20 0.3512 2.0417
338.20 0.4014 2.1219
338.20 0.4516 2.1601
338.20 0.5017 2.1606
338.20 0.5518 2.1247
338.20 0.6016 2.0478
338.20 0.6513 1.937
338.20 0.7008 1.7838
338.20 0.8016 1.3617
338.20 0.9010 0.7759
348.20 0.1005 0.9399
348.20 0.2010 1.5442
348.20 0.3010 1.9341
348.20 0.3512 2.0554
348.20 0.4014 2.131
348.20 0.4516 2.1731
348.20 0.5017 2.1761
348.20 0.5518 2.1332
348.20 0.6016 2.0584
348.20 0.6513 1.9531
348.20 0.7008 1.7899
348.20 0.8016 1.3781
348.20 0.9010 0.7837

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetophenone (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.20 0.1005 0.6958
298.20 0.2010 1.1021
298.20 0.3010 1.3661
298.20 0.3512 1.4489
298.20 0.4014 1.5109
298.20 0.4516 1.5502
298.20 0.5017 1.5673
298.20 0.5518 1.5614
298.20 0.6016 1.5328
298.20 0.6513 1.4795
298.20 0.7008 1.4005
298.20 0.8016 1.1346
298.20 0.9010 0.6842
313.20 0.1005 0.8039
313.20 0.2010 1.3046
313.20 0.3010 1.63
313.20 0.3512 1.732
313.20 0.4014 1.8068
313.20 0.4516 1.8517
313.20 0.5017 1.8663
313.20 0.5518 1.8521
313.20 0.6016 1.8084
313.20 0.6513 1.7354
313.20 0.7008 1.626
313.20 0.8016 1.2766
313.20 0.9010 0.7414
328.20 0.1005 0.9176
328.20 0.2010 1.4909
328.20 0.3010 1.8798
328.20 0.3512 1.9901
328.20 0.4014 2.0685
328.20 0.4516 2.1068
328.20 0.5017 2.1136
328.20 0.5518 2.0832
328.20 0.6016 2.0162
328.20 0.6513 1.9069
328.20 0.7008 1.7708
328.20 0.8016 1.3564
328.20 0.9010 0.7646
338.20 0.1005 0.9335
338.20 0.2010 1.5373
338.20 0.3010 1.9258
338.20 0.3512 2.0417
338.20 0.4014 2.1219
338.20 0.4516 2.1601
338.20 0.5017 2.1606
338.20 0.5518 2.1247
338.20 0.6016 2.0478
338.20 0.6513 1.937
338.20 0.7008 1.7838
338.20 0.8016 1.3617
338.20 0.9010 0.7759
348.20 0.1005 0.9399
348.20 0.2010 1.5442
348.20 0.3010 1.9341
348.20 0.3512 2.0554
348.20 0.4014 2.131
348.20 0.4516 2.1731
348.20 0.5017 2.1761
348.20 0.5518 2.1332
348.20 0.6016 2.0584
348.20 0.6513 1.9531
348.20 0.7008 1.7899
348.20 0.8016 1.3781
348.20 0.9010 0.7837

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 472.25
0.2960 403.15
0.3540 399.31
0.4560 394.15
0.5570 391.15
0.6270 389.15
0.6770 388.65
0.7160 388.15
0.7460 387.15
0.7710 386.15
0.7910 385.15
0.8080 384.65
0.8220 384.15
0.8550 383.65
0.8940 382.65
0.9550 380.65
1.0000 379.65

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 472.25
0.2960 403.15
0.3540 399.31
0.4560 394.15
0.5570 391.15
0.6270 389.15
0.6770 388.65
0.7160 388.15
0.7460 387.15
0.7710 386.15
0.7910 385.15
0.8080 384.65
0.8220 384.15
0.8550 383.65
0.8940 382.65
0.9550 380.65
1.0000 379.65

Sources