Mixture of 1-Propanol + Acetophenone

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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 (1) [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas
0.0000 0.0000
0.1470 0.8560
0.2570 0.9240
0.3410 0.9330
0.4090 0.9610
0.4640 0.9670
0.5090 0.9770
0.5470 0.9810
0.6090 0.9830
0.6550 0.9860
0.7080 0.9880
0.7460 0.9900
0.7760 0.9920
0.9330 0.9950
0.9500 0.9980
1.0000 1.0000

Mole fraction of 1-Propanol (1) [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas
0.0000 0.0000
0.1470 0.8560
0.2570 0.9240
0.3410 0.9330
0.4090 0.9610
0.4640 0.9670
0.5090 0.9770
0.5470 0.9810
0.6090 0.9830
0.6550 0.9860
0.7080 0.9880
0.7460 0.9900
0.7760 0.9920
0.9330 0.9950
0.9500 0.9980
1.0000 1.0000

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetophenone (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0997 0.5895
298.15 0.2003 0.9521
298.15 0.3002 1.1776
298.15 0.3505 1.2573
298.15 0.3998 1.3133
298.15 0.4501 1.3491
298.15 0.5003 1.3644
298.15 0.5499 1.3621
298.15 0.6004 1.3361
298.15 0.7003 1.2181
298.15 0.8006 0.9913
298.15 0.9002 0.6015
313.15 0.0997 0.6603
313.15 0.2003 1.0913
313.15 0.3002 1.3682
313.15 0.3505 1.4627
313.15 0.3998 1.5257
313.15 0.4501 1.5651
313.15 0.5003 1.5791
313.15 0.5499 1.569
313.15 0.6004 1.5311
313.15 0.7003 1.3732
313.15 0.8006 1.0825
313.15 0.9002 0.6307
328.15 0.0997 0.7287
328.15 0.2003 1.2339
328.15 0.3002 1.565
328.15 0.3505 1.6726
328.15 0.3998 1.745
328.15 0.4501 1.7893
328.15 0.5003 1.8062
328.15 0.5499 1.7863
328.15 0.6004 1.7419
328.15 0.7003 1.551
328.15 0.8006 1.2073
328.15 0.9002 0.6944
338.15 0.0997 0.7847
338.15 0.2003 1.3162
338.15 0.3002 1.6557
338.15 0.3505 1.7699
338.15 0.3998 1.8467
338.15 0.4501 1.8895
338.15 0.5003 1.8999
338.15 0.5499 1.8795
338.15 0.6004 1.8219
338.15 0.7003 1.6077
338.15 0.8006 1.2418
338.15 0.9002 0.7053
348.15 0.0997 0.8029
348.15 0.2003 1.3547
348.15 0.3002 1.7143
348.15 0.3505 1.8279
348.15 0.3998 1.9042
348.15 0.4501 1.9463
348.15 0.5003 1.9543
348.15 0.5499 1.9287
348.15 0.6004 1.8673
348.15 0.7003 1.6394
348.15 0.8006 1.2586
348.15 0.9002 0.7203

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetophenone (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0997 0.5895
298.15 0.2003 0.9521
298.15 0.3002 1.1776
298.15 0.3505 1.2573
298.15 0.3998 1.3133
298.15 0.4501 1.3491
298.15 0.5003 1.3644
298.15 0.5499 1.3621
298.15 0.6004 1.3361
298.15 0.7003 1.2181
298.15 0.8006 0.9913
298.15 0.9002 0.6015
313.15 0.0997 0.6603
313.15 0.2003 1.0913
313.15 0.3002 1.3682
313.15 0.3505 1.4627
313.15 0.3998 1.5257
313.15 0.4501 1.5651
313.15 0.5003 1.5791
313.15 0.5499 1.569
313.15 0.6004 1.5311
313.15 0.7003 1.3732
313.15 0.8006 1.0825
313.15 0.9002 0.6307
328.15 0.0997 0.7287
328.15 0.2003 1.2339
328.15 0.3002 1.565
328.15 0.3505 1.6726
328.15 0.3998 1.745
328.15 0.4501 1.7893
328.15 0.5003 1.8062
328.15 0.5499 1.7863
328.15 0.6004 1.7419
328.15 0.7003 1.551
328.15 0.8006 1.2073
328.15 0.9002 0.6944
338.15 0.0997 0.7847
338.15 0.2003 1.3162
338.15 0.3002 1.6557
338.15 0.3505 1.7699
338.15 0.3998 1.8467
338.15 0.4501 1.8895
338.15 0.5003 1.8999
338.15 0.5499 1.8795
338.15 0.6004 1.8219
338.15 0.7003 1.6077
338.15 0.8006 1.2418
338.15 0.9002 0.7053
348.15 0.0997 0.8029
348.15 0.2003 1.3547
348.15 0.3002 1.7143
348.15 0.3505 1.8279
348.15 0.3998 1.9042
348.15 0.4501 1.9463
348.15 0.5003 1.9543
348.15 0.5499 1.9287
348.15 0.6004 1.8673
348.15 0.7003 1.6394
348.15 0.8006 1.2586
348.15 0.9002 0.7203

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 472.25
0.1470 413.15
0.2570 400.65
0.3410 392.15
0.4090 388.15
0.4640 385.15
0.5090 383.15
0.5470 382.15
0.6090 380.15
0.6550 379.15
0.7080 377.15
0.7460 376.15
0.7760 374.15
0.9330 369.65
0.9500 369.15
1.0000 368.65

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 472.25
0.1470 413.15
0.2570 400.65
0.3410 392.15
0.4090 388.15
0.4640 385.15
0.5090 383.15
0.5470 382.15
0.6090 380.15
0.6550 379.15
0.7080 377.15
0.7460 376.15
0.7760 374.15
0.9330 369.65
0.9500 369.15
1.0000 368.65

Sources