Mixture of Isopropyl Alcohol + Acetophenone

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (2)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (2)
6. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Isopropyl Alcohol (1) [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000	0.0000
0.1450	0.8770
0.2530	0.9480
0.3360	0.9620
0.4030	0.9710
0.4580	0.9760
0.5030	0.9830
0.5420	0.9860
0.5750	0.9870
0.6030	0.9880
0.6500	0.9900
0.7170	0.9940
0.8090	0.9960
0.9310	0.9990
1.0000	1.0000

Mole fraction of Isopropyl Alcohol (1) [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000	0.0000
0.1450	0.8770
0.2530	0.9480
0.3360	0.9620
0.4030	0.9710
0.4580	0.9760
0.5030	0.9830
0.5420	0.9860
0.5750	0.9870
0.6030	0.9880
0.6500	0.9900
0.7170	0.9940
0.8090	0.9960
0.9310	0.9990
1.0000	1.0000

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetophenone (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0020
0.0892	0.0017
0.1658	0.0015
0.2517	0.0014
0.3432	0.0014
0.4297	0.0014
0.5345	0.0014
0.6466	0.0014
0.7561	0.0015
0.8635	0.0016
0.9568	0.0016
1.0000	0.0017

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetophenone (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0020
0.0892	0.0017
0.1658	0.0015
0.2517	0.0014
0.3432	0.0014
0.4297	0.0014
0.5345	0.0014
0.6466	0.0014
0.7561	0.0015
0.8635	0.0016
0.9568	0.0016
1.0000	0.0017

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	0.1000	0.7093
298.15	0.2001	1.1352
298.15	0.2996	1.3877
298.15	0.3502	1.4709
298.15	0.3995	1.5273
298.15	0.4497	1.5608
298.15	0.4996	1.5703
298.15	0.5503	1.5602
298.15	0.6003	1.5235
298.15	0.7006	1.3758
298.15	0.7994	1.1123
298.15	0.9005	0.6733
313.15	0.1000	0.8232
313.15	0.2001	1.3219
313.15	0.2996	1.6348
313.15	0.3502	1.7328
313.15	0.3995	1.7981
313.15	0.4497	1.8356
313.15	0.4996	1.8433
313.15	0.5503	1.8234
313.15	0.6003	1.7723
313.15	0.7006	1.5823
313.15	0.7994	1.2467
313.15	0.9005	0.7258
328.15	0.1000	0.8860
328.15	0.2001	1.4488
328.15	0.2996	1.788
328.15	0.3502	1.9026
328.15	0.3995	1.9737
328.15	0.4497	2.0141
328.15	0.4996	2.0188
328.15	0.5503	1.9915
328.15	0.6003	1.9277
328.15	0.7006	1.701
328.15	0.7994	1.323
328.15	0.9005	0.7516
338.15	0.1000	0.8880
338.15	0.2001	1.477
338.15	0.2996	1.8338
338.15	0.3502	1.952
338.15	0.3995	2.0259
338.15	0.4497	2.0663
338.15	0.4996	2.0703
338.15	0.5503	2.0375
338.15	0.6003	1.9724
338.15	0.7006	1.7326
338.15	0.7994	1.3375
338.15	0.9005	0.7594
348.15	0.1000	0.8907
348.15	0.2001	1.4805
348.15	0.2996	1.8456
348.15	0.3502	1.9621
348.15	0.3995	2.0371
348.15	0.4497	2.0756
348.15	0.4996	2.0779
348.15	0.5503	2.0449
348.15	0.6003	1.9743
348.15	0.7006	1.7343
348.15	0.7994	1.3422
348.15	0.9005	0.7625

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	0.1000	0.7093
298.15	0.2001	1.1352
298.15	0.2996	1.3877
298.15	0.3502	1.4709
298.15	0.3995	1.5273
298.15	0.4497	1.5608
298.15	0.4996	1.5703
298.15	0.5503	1.5602
298.15	0.6003	1.5235
298.15	0.7006	1.3758
298.15	0.7994	1.1123
298.15	0.9005	0.6733
313.15	0.1000	0.8232
313.15	0.2001	1.3219
313.15	0.2996	1.6348
313.15	0.3502	1.7328
313.15	0.3995	1.7981
313.15	0.4497	1.8356
313.15	0.4996	1.8433
313.15	0.5503	1.8234
313.15	0.6003	1.7723
313.15	0.7006	1.5823
313.15	0.7994	1.2467
313.15	0.9005	0.7258
328.15	0.1000	0.8860
328.15	0.2001	1.4488
328.15	0.2996	1.788
328.15	0.3502	1.9026
328.15	0.3995	1.9737
328.15	0.4497	2.0141
328.15	0.4996	2.0188
328.15	0.5503	1.9915
328.15	0.6003	1.9277
328.15	0.7006	1.701
328.15	0.7994	1.323
328.15	0.9005	0.7516
338.15	0.1000	0.8880
338.15	0.2001	1.477
338.15	0.2996	1.8338
338.15	0.3502	1.952
338.15	0.3995	2.0259
338.15	0.4497	2.0663
338.15	0.4996	2.0703
338.15	0.5503	2.0375
338.15	0.6003	1.9724
338.15	0.7006	1.7326
338.15	0.7994	1.3375
338.15	0.9005	0.7594
348.15	0.1000	0.8907
348.15	0.2001	1.4805
348.15	0.2996	1.8456
348.15	0.3502	1.9621
348.15	0.3995	2.0371
348.15	0.4497	2.0756
348.15	0.4996	2.0779
348.15	0.5503	2.0449
348.15	0.6003	1.9743
348.15	0.7006	1.7343
348.15	0.7994	1.3422
348.15	0.9005	0.7625

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetophenone (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3745
0.0892	1.3971
0.1658	1.4181
0.2517	1.4393
0.3432	1.4601
0.4297	1.4775
0.5345	1.4953
0.6466	1.5099
0.7561	1.5195
0.8635	1.5255
0.9568	1.5276
1.0000	1.5308

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetophenone (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3745
0.0892	1.3971
0.1658	1.4181
0.2517	1.4393
0.3432	1.4601
0.4297	1.4775
0.5345	1.4953
0.6466	1.5099
0.7561	1.5195
0.8635	1.5255
0.9568	1.5276
1.0000	1.5308

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetophenone (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	780.98
0.0892	813.69
0.1658	839.2
0.2517	865.44
0.3432	890.91
0.4297	913.04
0.5345	937.56
0.6466	961.31
0.7561	982.35
0.8635	1001.26
0.9568	1016.5
1.0000	1023.3

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetophenone (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	780.98
0.0892	813.69
0.1658	839.2
0.2517	865.44
0.3432	890.91
0.4297	913.04
0.5345	937.56
0.6466	961.31
0.7561	982.35
0.8635	1001.26
0.9568	1016.5
1.0000	1023.3

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	472.25
0.1450	412.15
0.2530	391.65
0.3360	383.65
0.4030	378.65
0.4580	375.15
0.5030	371.15
0.5420	369.15
0.5750	367.15
0.6030	366.15
0.6500	364.15
0.7170	363.15
0.8090	360.65
0.9310	356.65
1.0000	353.84

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.2 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	472.25
0.1450	412.15
0.2530	391.65
0.3360	383.65
0.4030	378.65
0.4580	375.15
0.5030	371.15
0.5420	369.15
0.5750	367.15
0.6030	366.15
0.6500	364.15
0.7170	363.15
0.8090	360.65
0.9310	356.65
1.0000	353.84

Sources

• Isobaric Vapor Liquid Equilibrium Data for Binary Mixtures of 1-Phenylethanone with a Few Alcohols at 95.2 kPa
• Excess Molar Enthalpies of Acetophenone + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at Different Temperatures and Pressures
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols